JP4977694B2 - Multi-layer protective film co-extruded with a film layer comprising at least one ethylene-vinyl alcohol-copolymer (EVOH), method for producing the same and method for using the same - Google Patents
Multi-layer protective film co-extruded with a film layer comprising at least one ethylene-vinyl alcohol-copolymer (EVOH), method for producing the same and method for using the same Download PDFInfo
- Publication number
- JP4977694B2 JP4977694B2 JP2008513968A JP2008513968A JP4977694B2 JP 4977694 B2 JP4977694 B2 JP 4977694B2 JP 2008513968 A JP2008513968 A JP 2008513968A JP 2008513968 A JP2008513968 A JP 2008513968A JP 4977694 B2 JP4977694 B2 JP 4977694B2
- Authority
- JP
- Japan
- Prior art keywords
- layer
- film
- ethylene
- protective film
- vinyl alcohol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 title claims abstract description 109
- 239000004715 ethylene vinyl alcohol Substances 0.000 title claims abstract description 10
- 230000001681 protective effect Effects 0.000 title claims description 53
- 238000000034 method Methods 0.000 title claims description 23
- 238000004519 manufacturing process Methods 0.000 title claims description 16
- 239000010410 layer Substances 0.000 claims abstract description 238
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 47
- 239000005977 Ethylene Substances 0.000 claims abstract description 47
- 229920000098 polyolefin Polymers 0.000 claims abstract description 38
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 28
- 239000001301 oxygen Substances 0.000 claims abstract description 28
- 238000004806 packaging method and process Methods 0.000 claims abstract description 16
- 235000013305 food Nutrition 0.000 claims abstract description 4
- 239000002346 layers by function Substances 0.000 claims abstract description 3
- -1 polypropylene Polymers 0.000 claims description 63
- 229920001155 polypropylene Polymers 0.000 claims description 55
- 239000004743 Polypropylene Substances 0.000 claims description 52
- 239000000463 material Substances 0.000 claims description 26
- 239000011241 protective layer Substances 0.000 claims description 24
- 229920001577 copolymer Polymers 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 14
- 239000013638 trimer Substances 0.000 claims description 13
- 229920000642 polymer Polymers 0.000 claims description 11
- 239000012790 adhesive layer Substances 0.000 claims description 9
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 239000000155 melt Substances 0.000 claims description 6
- 229920000573 polyethylene Polymers 0.000 claims description 6
- JRZJOMJEPLMPRA-UHFFFAOYSA-N 1-nonene Chemical compound CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 5
- 239000004698 Polyethylene Substances 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 5
- 230000005540 biological transmission Effects 0.000 claims description 4
- 238000001125 extrusion Methods 0.000 claims description 4
- 239000000049 pigment Substances 0.000 claims description 4
- 229920001384 propylene homopolymer Polymers 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims description 4
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 claims description 4
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 239000003205 fragrance Substances 0.000 claims description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical group O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 3
- 239000012785 packaging film Substances 0.000 claims description 3
- 229920006280 packaging film Polymers 0.000 claims description 3
- 238000007747 plating Methods 0.000 claims description 3
- 229920001748 polybutylene Polymers 0.000 claims description 3
- 238000007639 printing Methods 0.000 claims description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 3
- 229920006300 shrink film Polymers 0.000 claims description 3
- 229920001169 thermoplastic Polymers 0.000 claims description 3
- 239000004416 thermosoftening plastic Substances 0.000 claims description 3
- 239000013032 Hydrocarbon resin Substances 0.000 claims description 2
- 229920006270 hydrocarbon resin Polymers 0.000 claims description 2
- 239000010408 film Substances 0.000 claims 36
- 238000004581 coalescence Methods 0.000 claims 1
- 239000013039 cover film Substances 0.000 claims 1
- 230000004888 barrier function Effects 0.000 abstract description 17
- 230000035699 permeability Effects 0.000 abstract description 6
- 241000208125 Nicotiana Species 0.000 abstract 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 abstract 1
- 238000000605 extraction Methods 0.000 description 21
- 230000003287 optical effect Effects 0.000 description 12
- 229920005629 polypropylene homopolymer Polymers 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 9
- 239000000126 substance Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 229920006378 biaxially oriented polypropylene Polymers 0.000 description 4
- 239000011127 biaxially oriented polypropylene Substances 0.000 description 4
- RZXDTJIXPSCHCI-UHFFFAOYSA-N hexa-1,5-diene-2,5-diol Chemical compound OC(=C)CCC(O)=C RZXDTJIXPSCHCI-UHFFFAOYSA-N 0.000 description 4
- 229920001903 high density polyethylene Polymers 0.000 description 4
- 239000004700 high-density polyethylene Substances 0.000 description 4
- 229920000728 polyester Polymers 0.000 description 4
- 229920000139 polyethylene terephthalate Polymers 0.000 description 4
- 239000005020 polyethylene terephthalate Substances 0.000 description 4
- 239000004594 Masterbatch (MB) Substances 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 239000012792 core layer Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 239000002985 plastic film Substances 0.000 description 3
- 229920006255 plastic film Polymers 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000004224 protection Effects 0.000 description 3
- 229920002397 thermoplastic olefin Polymers 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical group OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000005524 ceramic coating Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920005638 polyethylene monopolymer Polymers 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 239000005033 polyvinylidene chloride Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 2
- 229910052814 silicon oxide Inorganic materials 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 229920003313 Bynel® Polymers 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- 229920003354 Modic® Polymers 0.000 description 1
- 229920003300 Plexar® Polymers 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 230000002457 bidirectional effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 239000000976 ink Substances 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 229920006113 non-polar polymer Polymers 0.000 description 1
- 239000012766 organic filler Substances 0.000 description 1
- 239000011146 organic particle Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- 230000003711 photoprotective effect Effects 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920006267 polyester film Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/10—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
- B29C55/12—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
- B29C55/16—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial simultaneously
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
- B29C48/185—Articles comprising two or more components, e.g. co-extruded layers the components being layers comprising six or more components, i.e. each component being counted once for each time it is present, e.g. in a layer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/023—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets using multilayered plates or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
- B32B27/306—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl acetate or vinyl alcohol (co)polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/42—Component parts, details or accessories; Auxiliary operations
- B29C49/42394—Providing specific wall thickness
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/08—Copolymers of ethylene
- B29K2023/086—EVOH, i.e. ethylene vinyl alcohol copolymer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2029/00—Use of polyvinylalcohols, polyvinylethers, polyvinylaldehydes, polyvinylketones or polyvinylketals or derivatives thereof as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2250/00—Layers arrangement
- B32B2250/05—5 or more layers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2250/00—Layers arrangement
- B32B2250/24—All layers being polymeric
- B32B2250/246—All polymers belonging to those covered by groups B32B27/32 and B32B27/30
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/724—Permeability to gases, adsorption
- B32B2307/7242—Non-permeable
- B32B2307/7244—Oxygen barrier
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/724—Permeability to gases, adsorption
- B32B2307/7242—Non-permeable
- B32B2307/7246—Water vapor barrier
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/724—Permeability to gases, adsorption
- B32B2307/7242—Non-permeable
- B32B2307/7248—Odour barrier
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/75—Printability
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2553/00—Packaging equipment or accessories not otherwise provided for
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24942—Structurally defined web or sheet [e.g., overall dimension, etc.] including components having same physical characteristic in differing degree
- Y10T428/2495—Thickness [relative or absolute]
- Y10T428/24967—Absolute thicknesses specified
- Y10T428/24975—No layer or component greater than 5 mils thick
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/26—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/26—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
- Y10T428/269—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension including synthetic resin or polymer layer or component
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Laminated Bodies (AREA)
- Wrappers (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
Description
本発明は、フィルムを構成する重合体として結晶性ポリオレフィンを使用し、更に、少なくとも1つのエチレン−ビニルアルコール共重合体(EVOH)から成る同時押出成形された層を機能層又は保護層として有し、二軸方向性フィルムにより十分に機械的特性を選定した多層フィルムの形態であり、包装用、特に食料品、嗜好品及び他の傷つき易い商品の包装用の保護フィルムに関する。 The present invention uses crystalline polyolefin as a polymer constituting the film, and further has a coextruded layer composed of at least one ethylene-vinyl alcohol copolymer (EVOH) as a functional layer or a protective layer. The invention relates to a protective film for packaging, particularly for packaging foodstuffs, luxury goods and other sensitive products, in the form of a multilayer film with sufficient mechanical properties selected by a biaxially oriented film.
本発明は、更に前記フィルムの製造方法、包装、特に傑出するフィルムの光学特性、強度特性、保護特性及び必要に応じて収縮特性を利用する食料品及び嗜好品を包装するフィルムの使用方法に関する。 The present invention further relates to a method for producing said film, packaging, and in particular a method for using a film for packaging foodstuffs and taste products utilizing the optical properties, strength properties, protective properties and optionally shrinkage properties of outstanding films.
プラスチックフィルムをベースとする包装は、最早現代の食料品に不可欠であると思われる。包装すべき商品に応じて、プラスチックフィルムに種々の要求が発生する。その際、食料品及び嗜好品の包装用プラスチックフィルムでは、販売経路及び食料品の消費までの末端消費者に対して、包装された食料品又は嗜好品の安定性を保証する特性が注目される。 Packaging based on plastic film is now considered essential for modern food products. Depending on the product to be packaged, various demands arise on the plastic film. At that time, in the plastic film for packaging of foodstuffs and luxury goods, attention is paid to the characteristic that guarantees the stability of the packaged foodstuffs or luxury goods for the end-users until the sales channel and the consumption of the foodstuffs. .
包装フィルムに高い要求が発生すると、現在の食料品及び嗜好品の分野では、良好な強度、良好な光学特性及び光沢のある特にアルミニウム製の金属フィルム又は特に酸化珪素(SiOx)又は酸化アルミニウム(AlOx)から成る透明なセラミック被覆用の良好な被覆特性を有するポリエステルベースフィルム(PET、ポリエチレンテレフタレート)を使用することが多い。薄い金属又はセラミックフィルムは、特に水蒸気に対する透過性(水蒸気透過率、WVTR、g/(m2d)即ちg/(m2/24h)で測定、ASTM-E96)及び酸素(酸素透過率、OTR、cm3/(m2dbar)即ち1barの気圧におけるcm3/(m224h)で測定、ASTM-3985)に対して、フィルムへの高い要求を満足できる保護特性を与える。包装調製に必要なフィルムの溶着可能性又は密閉可能性を確実に付与するため、追加の外側ポリオレフィン層、例えば金属被覆又はセラミック被覆を有する例えば高密度ポリエチレン(HDPE)又は低密度ポリエチレン(LDPE)から成るポリエチレン層が通常設けられる。このポリエステルフィルムは、高い品質要求を満足するが、特にポリエステル重合体が比較的高価でありかつ比較的高い密度を有する難点がある。 Due to the high demands on packaging films, the current food and luxury goods sector has good strength, good optical properties and glossy metal films, especially made of aluminum or especially silicon oxide (SiO x ) or aluminum oxide ( Polyester base films (PET, polyethylene terephthalate) with good coating properties for transparent ceramic coatings composed of AlO x ) are often used. Thin metal or ceramic films are especially permeable to water vapor (water vapor transmission rate, WVTR, measured in g / (m 2 d) or g / (m 2 / 24h), ASTM-E96) and oxygen (oxygen transmission rate, OTR). , Measured at cm 3 / (m 2 dbar), i.e. cm 3 / (m 2 24h) at 1 bar pressure, ASTM-3985) provides protective properties that can satisfy the high demands on the film. To ensure the film's weldability or sealability required for packaging preparation, from an additional outer polyolefin layer such as high density polyethylene (HDPE) or low density polyethylene (LDPE) with a metal or ceramic coating A polyethylene layer is usually provided. This polyester film satisfies high quality requirements, but in particular has a drawback that the polyester polymer is relatively expensive and has a relatively high density.
従って、ポリ塩化ビニリデン(PVDC)又は酸化珪素(SiOx)を備える間接製造工程(オフライン)で積層された二軸ポリエチレンテレフタレート(BOPET)フィルムの代わりに、直接製造工程(インライン)で同時押出成形されたポリオレフィンフィルム、特にポリプロピレンフィルムに頼ることが試みられた。前記フィルムは、(保護フィルムとしても)比較的安く製造できる。しかしながら、より高価ではあるが品質の高い二軸ポリエチレンテレフタレート(BOPET)フィルムと競合するには、光学特性、強度特性及び保護特性でも、ポリオレフィンフィルムに重大な欠点があってはならない。 Therefore, instead of biaxial polyethylene terephthalate (BOPET) film laminated in an indirect manufacturing process (offline) with polyvinylidene chloride (PVDC) or silicon oxide (SiO x ), it is co-extruded in a direct manufacturing process (inline) Attempts have been made to rely on other polyolefin films, especially polypropylene films. The film can be manufactured relatively cheaply (even as a protective film). However, to compete with the more expensive but higher quality biaxial polyethylene terephthalate (BOPET) film, the polyolefin film must also have no significant drawbacks in terms of optical properties, strength properties and protective properties.
例えばポリエチレン、ポリプロピレン又はその他のオレフィンとの共重合体をベースとするポリオレフィン層と、良好な保護特性として公知のエチレン−ビニルアルコール共重合体(EVOH)から成る層とを保護フィルム内で組合せることが公知である。また、空気の湿度の進入の際にその保護特性が悪化するので、エチレン−ビニルアルコール共重合体層を通常多層フィルムの芯に配置して、エチレン−ビニルアルコール共重合体層をポリオレフィン層の両面で周囲に対して好ましく遮蔽することも知られている。 For example, combining a polyolefin layer based on a copolymer of polyethylene, polypropylene or other olefins with a layer made of an ethylene-vinyl alcohol copolymer (EVOH) known as good protective properties in a protective film Is known. In addition, since the protective properties deteriorate when air humidity enters, an ethylene-vinyl alcohol copolymer layer is usually placed on the core of the multilayer film, and the ethylene-vinyl alcohol copolymer layer is disposed on both sides of the polyolefin layer. It is also known to shield preferably from the surroundings.
また、エチレン−ビニルアルコール共重合体内でのビニルアルコール群のモル濃度がエチレン群のモル濃度に対して十分に高く、エチレン−ビニルアルコール共重合体層の保護特性が通常改善されることが重要である。しかしながら、共重合体内の極性ビニルアルコール群の濃度が増加するに伴い、ポリオレフィン等の無極性重合体に対する不耐性も増大する。 It is also important that the molar concentration of the vinyl alcohol group in the ethylene-vinyl alcohol copolymer is sufficiently high relative to the molar concentration of the ethylene group, and that the protective properties of the ethylene-vinyl alcohol copolymer layer are usually improved. is there. However, as the concentration of the polar vinyl alcohol group in the copolymer increases, the intolerance to nonpolar polymers such as polyolefins also increases.
更に、二軸延伸(二軸方向性付与)によりポリオレフィンフィルムの機械的特性及び光学特性を改善し、二軸延伸によりエチレン−ビニルアルコール共重合体保護層の保護特性も改善できることが知られている。 Furthermore, it is known that the mechanical properties and optical properties of the polyolefin film can be improved by biaxial stretching (providing biaxial orientation), and the protective properties of the ethylene-vinyl alcohol copolymer protective layer can also be improved by biaxial stretching. .
しかしながら、同様に、ポリオレフィン層、特にポリプロピレン層とエチレン−ビニルアルコール共重合体層とが互いに直接接触して良好には粘着せず、非親和性(非接着性)を有し、延伸の際に種々の層が種々の方法で結晶化して、異なる条件の下で所望の光学特性を構成することが知られている。従って、ポリオレフィンとエチレン−ビニルアルコール共重合体層との同時延伸が容易となり又は一定の場合に全般的にまず同時延伸を可能にする粘着層として作用する特別に変性(改質)ポリオレフィン製の特別の中間層を設けて、層の相性又は親和性を改善することが一般的に知られている。 However, similarly, the polyolefin layer, in particular, the polypropylene layer and the ethylene-vinyl alcohol copolymer layer are in direct contact with each other and do not adhere well and have non-affinity (non-adhesiveness). It is known that different layers crystallize in different ways to form the desired optical properties under different conditions. Thus, specially made of specially modified (modified) polyolefins that facilitate the simultaneous stretching of the polyolefin and the ethylene-vinyl alcohol copolymer layer or act as an adhesive layer that generally allows simultaneous stretching in certain cases in general. It is generally known to provide intermediate layers to improve the compatibility or affinity of the layers.
にもかかわらず、エチレン−ビニルアルコール共重合体保護層を備える多層ポリオレフィンフィルムの二軸方向性付与の際に、種々の条件の下で最適な光学特性、強度特性及び良好な保護特性が構成されるので、更に対向して作用する効果を調整しなければならない。重要な従来技術は、この問題を提起し、達成可能な所望の特性に対する極力良好な妥協を示すエチレン−ビニルアルコール共重合体保護層を備える多層ポリオレフィンフィルムを製造する種々の方針を追求する。 Nevertheless, the optimal optical properties, strength properties, and good protective properties under various conditions are formed when biaxiality is imparted to the multilayer polyolefin film provided with an ethylene-vinyl alcohol copolymer protective layer. Therefore, the effect of acting oppositely must be adjusted. Important prior art poses this problem and pursues various strategies to produce multilayer polyolefin films with an ethylene-vinyl alcohol copolymer protective layer that exhibits the best possible compromise to the achievable desired properties.
特許文献1は、エチレン−ビニルアルコール共重合体芯層を備える多層初期フィルム及び二つのポリオレフィン−外側層をほぼ130℃〜140℃の温度範囲でまず長手方向(機械方向MD)に延伸し、次に、ほぼ150℃〜160℃の範囲に変更温度条件の下で、横方向(横断方向TD)に延伸することにより、二方向に順次延伸する方法を開示する。得られる面積延伸比は、僅か6(2×3)〜28(4×7)なる比較的僅かな面積増大の範囲にある。また、一般的に25〜75モル%、エチレン濃度のエチレン−ビニルアルコール共重合体が公知であるが、少なくとも45モル%のエチレンモル濃度のエチレン−ビニルアルコール共重合体を使用して、延伸に対する十分な可撓性をエチレン−ビニルアルコール共重合体に付与して保護フィルムの二軸延伸を行うべきことを示す。20℃で0%の相対湿度では、12〜13cm3/m2dの範囲の酸素透過率(OTR)を有する多層フィルムが得られた。 In Patent Document 1, a multilayer initial film having an ethylene-vinyl alcohol copolymer core layer and two polyolefin-outer layers are first stretched in a longitudinal direction (machine direction MD) in a temperature range of about 130 ° C. to 140 ° C. In addition, a method of sequentially stretching in two directions by stretching in the transverse direction (transverse direction TD) under a changing temperature condition in a range of approximately 150 ° C. to 160 ° C. is disclosed. The area stretch ratio obtained is in the range of a relatively slight area increase of only 6 (2 × 3) to 28 (4 × 7). In general, an ethylene-vinyl alcohol copolymer having an ethylene concentration of 25 to 75 mol% is known, but an ethylene-vinyl alcohol copolymer having an ethylene mol concentration of at least 45 mol% is used, and sufficient for stretching. It indicates that the protective film should be biaxially stretched by imparting such flexibility to the ethylene-vinyl alcohol copolymer. A multilayer film having an oxygen transmission rate (OTR) in the range of 12-13 cm 3 / m 2 d was obtained at 20 ° C. and 0% relative humidity.
特許文献2は、同様に二軸方向に35〜70倍のより高い面積増大で同様のフィルムを順次延伸し、機械方向に温度140乃至150℃の範囲で延伸し、横方向に温度160〜170℃の範囲で延伸する同様の方法を示す。再び、エチレン−ビニルアルコール共重合体中のエチレン濃度を少なくとも45%にして、延伸の際に十分な効果を得ることを示す。 Similarly, Patent Document 2 similarly stretches the same film in the biaxial direction with a higher area increase of 35 to 70 times, stretches the film in the machine direction at a temperature of 140 to 150 ° C., and laterally stretches the temperature in the range of 160 to 170. A similar method of stretching in the range of ° C. is shown. Again, the ethylene concentration in the ethylene-vinyl alcohol copolymer is set to at least 45%, indicating that a sufficient effect is obtained during stretching.
特許文献3は、49〜64倍の面積拡大比で同時延伸として比較例のエチレン−ビニルアルコール共重合体保護層を備えるポリプロピレンベースの多層フィルムの延伸する一般的な形態を提案するが、その際、実際には唯一の実施の形態の記述も説明もなく、特許文献3は、各層に対する重合体品質に使用する延伸の実施条件が「同時延伸」と理解される。同様に、フィルム品質に対するより正確な記載を欠く。従って、特許文献3は、全体として専門家に具体的な実施可能な要件を示していない。 Patent Document 3 proposes a general form of stretching a polypropylene-based multilayer film having a protective layer of an ethylene-vinyl alcohol copolymer of a comparative example as simultaneous stretching at an area expansion ratio of 49 to 64 times. Actually, there is no description or explanation of the only embodiment, and in Patent Document 3, it is understood that the conditions for stretching used for the polymer quality for each layer are “simultaneous stretching”. Similarly, a more accurate description of film quality is lacking. Therefore, Patent Document 3 does not show specific practicable requirements for experts as a whole.
当該専門家の知識から出発して、範囲49〜64の面積延伸比でポリプロピレンに二軸延伸を行うため、所定の延伸温度を保持すべきであり、特許文献3の記載に対応する公知の適宜の温度範囲内で、40モル%以下のエチレンモル濃度であるエチレン−ビニルアルコール共重合体芯層を備えるポリプロピレンベースの多層フィルムを同時に二軸方向に延伸し方向性の付与を試して、延伸を発生する結晶化に基づくエチレン−ビニルアルコール共重合体層の引裂(網目構造の構成)を観察できる。エチレン−ビニルアルコール共重合体層に引裂が発生すると、最早必然的に良好な保護特性が低下して、フィルム品質が全体として不十分となる。この場合、従来の延伸パラメータを利用する特許文献3での延伸は、光学特性及び保護特性が機能しないフィルムとなる。 Starting from the knowledge of the expert, in order to perform biaxial stretching on polypropylene with an area stretch ratio in the range 49-64, a predetermined stretching temperature should be maintained, and a known appropriate one corresponding to the description in Patent Document 3 Within the temperature range, a polypropylene-based multilayer film having an ethylene-vinyl alcohol copolymer core layer having an ethylene molar concentration of 40 mol% or less is stretched biaxially at the same time to give directionality, and stretching is generated. It is possible to observe tearing (configuration of network structure) of the ethylene-vinyl alcohol copolymer layer based on crystallization. When tearing occurs in the ethylene-vinyl alcohol copolymer layer, the protective properties are inevitably deteriorated and the film quality as a whole becomes insufficient. In this case, the stretching in Patent Document 3 using conventional stretching parameters results in a film in which the optical properties and the protective properties do not function.
特許文献4は、付着剤としてエチレン−ビニルアルコール共重合体層及びポリオレフィン層の間にも適する所定の変性ポリオレフィンを示す。僅かなエチレン濃度、当該発明による付着剤層及び44モル%のエチレン濃度のエチレン−ビニルアルコール共重合体層を有するポリプロピレン層を備える多層テストフィルムは、付着強度の試験の例では、80℃で僅か9倍の増大面積に順次延伸される。付着に関する他の記載は、テストフィルムの他の特性に対する如何なる記載も存在しない。 Patent Document 4 shows a predetermined modified polyolefin which is also suitable as an adhesive between the ethylene-vinyl alcohol copolymer layer and the polyolefin layer. A multi-layer test film comprising a polypropylene layer having a slight ethylene concentration, an adhesive layer according to the invention and an ethylene-vinyl alcohol copolymer layer having an ethylene concentration of 44 mol%, is a Sequentially stretched to 9 times increased area. There is no other description of adhesion regarding the other properties of the test film.
特許文献5及び特許文献6は、同様に、エチレン−ビニルアルコール共重合体保護層を内側に備える多層ポリオレフィンフィルムの二軸方向性付与を示すより最近の2件の特許出願である。 Patent Document 5 and Patent Document 6 are two more recent patent applications that similarly show biaxial orientation of a multilayer polyolefin film having an ethylene-vinyl alcohol copolymer protective layer on the inside.
特許文献5は、熱可塑性多層二軸方向性収縮フィルムを示す。中間層は、エチレン−ビニルアルコール−共重合体から成り、外側層は、ポリエチレン−単独重合体又は共重合体から成る。同時延伸される多層フィルムは、機械方向にも横方向にも4倍以上の延伸比が好適である。MD×TDの延伸比を4.5×4.5又は5×5にする例は、延伸時に20.25倍又は25倍の面積増大に相当する。 Patent document 5 shows a thermoplastic multilayer biaxial direction shrink film. The intermediate layer is made of ethylene-vinyl alcohol-copolymer, and the outer layer is made of polyethylene-homopolymer or copolymer. The multilayer film that is simultaneously stretched preferably has a stretch ratio of 4 times or more both in the machine direction and in the transverse direction. An example in which the MD × TD stretch ratio is 4.5 × 4.5 or 5 × 5 corresponds to an area increase of 20.25 times or 25 times during stretching.
外側層内のポリエチレン−単独重合体又は共重合体を使用すると、熱安定性フィルムを製造できず、開示される方法条件は、ポリプロピレンベースのフィルムの加工に直接転用することができない。また、ほぼ28からほぼ48モル%の範囲のエチレン濃度のエチレン−ビニルアルコール共重合体品質を一般的に使用できることを示す。しかしながら、公知の従来技術と同様に、44モル%のエチレン濃度のエチレン−ビニルアルコール共重合体のみを全例に使用する。 If a polyethylene-homopolymer or copolymer in the outer layer is used, a heat-stable film cannot be produced and the disclosed process conditions cannot be directly transferred to the processing of polypropylene-based films. It also indicates that ethylene-vinyl alcohol copolymer qualities with an ethylene concentration in the range of approximately 28 to approximately 48 mol% can be used generally. However, as in the known prior art, only an ethylene-vinyl alcohol copolymer having an ethylene concentration of 44 mol% is used in all examples.
特許文献6は、ポリプリピレン、付着剤及びエチレン−ビニルアルコール共重合体の複合材から成り、二軸方向に順次延伸する多層フィルムの製造法を示す。溶解物の形態で同一幅の層形態に複合材が同時押出成形される。続いて、フィルムは、まず長手方向(MD)に、その後横方向(TD)にクリップ台により延伸され、延伸時の温度は、機械方向に110〜165℃、特に140〜160℃の範囲にあり、機械方向に130〜180℃、好ましくは140〜180℃の範囲にある。当該発明の本質として、横延伸の際に全5層を台クリップにより共通にかつ同時に把持する点が指摘される。エチレン−ビニルアルコール共重合体層のみを把持すると、エチレン−ビニルアルコール共重合体層が引き裂かれて、フィルムが不良品となる。エチレン濃度44モル%のエチレン−ビニルアルコール共重合体を使用して、温度23℃、湿度50%で酸素遮断性約5cm3/m2dの最良酸素保護を備えて製造されるフィルムのエチレン−ビニルアルコール共重合体層の最終厚さは、ほぼ5μmである。 Patent document 6 shows the manufacturing method of the multilayer film which consists of a composite material of a polypropylene, an adhesive agent, and an ethylene-vinyl alcohol copolymer, and extends | stretches sequentially in a biaxial direction. The composite material is coextruded in the form of a layer of the same width in the form of a melt. Subsequently, the film is first stretched by a clip table in the longitudinal direction (MD) and then in the transverse direction (TD), and the temperature during stretching is in the range of 110-165 ° C, particularly 140-160 ° C in the machine direction. In the machine direction, it is 130 to 180 ° C, preferably 140 to 180 ° C. As the essence of the present invention, it is pointed out that all the five layers are gripped in common and simultaneously by the base clip during the transverse stretching. If only the ethylene-vinyl alcohol copolymer layer is gripped, the ethylene-vinyl alcohol copolymer layer is torn and the film becomes defective. An ethylene-vinyl alcohol copolymer having an ethylene concentration of 44 mol% is used to produce ethylene--of a film produced with the best oxygen protection with an oxygen barrier of about 5 cm 3 / m 2 d at a temperature of 23 ° C. and humidity of 50% The final thickness of the vinyl alcohol copolymer layer is approximately 5 μm.
本発明の課題は、低いエチレンのモル濃度を備えるエチレン−ビニルアルコール共重合体の有利な保護特性を完全に利用し、方向性ポリプロピレンフィルムの公知の有利な特性に加えて、特に酸素及び香料に対する改良された保護値と所望の強度とを有し、同時に透明でかつ光沢のある包装フィルムで、酸素、水蒸気、芳香及び臭気に対する傑出する不透過性を備えるフィルムを提供し、少なくとも1つのエチレン−ビニルアルコール共重合体保護層を備える二軸方向性のポリオレフィン層をベースとする改良された保護フィルム、その製造方法及び使用方法を提供することにある。 The object of the present invention is to take full advantage of the advantageous protective properties of ethylene-vinyl alcohol copolymers with low ethylene molar concentrations, in addition to the known advantageous properties of directional polypropylene films, in particular against oxygen and perfume. Providing a film having improved protection value and desired strength, at the same time transparent and glossy packaging film with outstanding impermeability to oxygen, water vapor, aroma and odor, and at least one ethylene- It is an object of the present invention to provide an improved protective film based on a biaxially oriented polyolefin layer provided with a vinyl alcohol copolymer protective layer, and a method for producing and using the same.
基本的かつ好適な特徴を有する請求項1〜18のフィルム、主たる特徴を備える請求項19〜21のフィルム製造方法及び請求項22及び23のフィルム使用方法により、この課題は、解決される。 This problem is solved by the film according to claims 1 to 18 having basic and preferred characteristics, the film production method according to claims 19 to 21 and the film use method according to claims 22 and 23 having the main characteristics.
頭記従来技術を引用しつつ当業者の専門知識を確認しかつ補完的に指摘しながら、本発明を以下より詳細に説明する。 The present invention will be described in more detail below, while confirming and complementarily pointing out the expertise of those skilled in the art with reference to the prior art.
通常の多層フィルムは、フィルムを構成する主重合体から成る少なくとも1つの基本的な機械的特性を決定する支持層と、所望の保護特性を達成する外側保護層又は内側保護層と、印刷可能性、被覆性又は密閉された包装の調製又は積層に必要な密閉性を生ずる外側層とを含む。 A typical multilayer film comprises a support layer that determines at least one basic mechanical property of the main polymer that makes up the film, an outer protective layer or inner protective layer that achieves the desired protective properties, and printability. And an outer layer that provides the necessary sealing properties for the preparation or lamination of the coated or sealed package.
本発明の範囲内において、層A/層B/層C/層D/層C/層B/層Eにより構成される7層構造を選択し、各層A、層B、層C、層D及び層Eを個々に以下詳細に説明する。 Within the scope of the present invention, a seven-layer structure constituted by layer A / layer B / layer C / layer D / layer C / layer B / layer E is selected, and each layer A, layer B, layer C, layer D and Layer E is described in detail below individually.
中心の内側保護層Dは、エチレン−ビニルアルコール−共重合体(EVOH)から成る。変性ポリオレフィン、特に変性ポリプロピレンから成る付着剤層Cは、内側保護層Dに隣接して両側に配置される。部分結晶性の熱可塑性ポリオレフィン又は部分結晶性の熱可塑性ポリオレフィンの混合体から成る構造層Bが付着剤層Cに隣接して配置され、二軸延伸に必要な温度条件に対して特別に選定し又は変性し、好ましくは同様にポリオレフィンベースの材料である。外側層A及びEは、同様に部分結晶性の熱可塑性ポリオレフィンから成り、それに関して実際には、選定基準は、二軸延伸後のその表面特性である。 The central inner protective layer D is made of ethylene-vinyl alcohol-copolymer (EVOH). Adhesive layers C made of modified polyolefins, in particular modified polypropylene, are arranged on both sides adjacent to the inner protective layer D. A structural layer B consisting of a partially crystalline thermoplastic polyolefin or a mixture of partially crystalline thermoplastic polyolefins is placed adjacent to the adhesive layer C and is specially selected for the temperature conditions required for biaxial stretching. Or modified and preferably a polyolefin-based material as well. The outer layers A and E are likewise composed of partially crystalline thermoplastic polyolefins, in which the actual selection criterion is their surface properties after biaxial stretching.
自体公知の方法により平坦ノズルから多層溶解物を同時押出成形し、得られる多層溶解物を冷却ローラに接触させて結合層を硬化させる。次に、同時延伸装置によりフィルムを延伸する。 A multilayer melt is coextruded from a flat nozzle by a method known per se, and the resulting multilayer melt is brought into contact with a cooling roller to cure the bonding layer. Next, the film is stretched by a simultaneous stretching apparatus.
同時延伸の実施に好適な方法は、リニアモータ駆動装置(LISIM(登録商標))を備える同時延伸装置で平面フィルムに延伸する方法である。しかしながら、機械的同時延伸装置(MSO;チェーン駆動装置を備える機械式同時延伸装置)によるあまり有利ではない同時延伸法及びバブル(BUBBLE)又はダブルバブル(DOUBLE-BUBBLE)法によるチューブフィルム延伸製造法も同様に本発明の範囲に含まれる。 A method suitable for carrying out the simultaneous stretching is a method in which the film is stretched to a flat film by a simultaneous stretching device equipped with a linear motor driving device (LISIM (registered trademark)). However, there is also a simultaneous film stretching method that is not very advantageous by mechanical simultaneous stretching device (MSO; mechanical simultaneous stretching device with chain drive) and tube film stretching method by bubble (BUBBLE) or double bubble (DOUBLE-BUBBLE) method. Similarly, it is included in the scope of the present invention.
同時延伸に通常の特性の二軸ポリプロピレンフィルムの場合に、本発明に通じる研究の範囲内で、エチレン濃度44モル%及び48モル%のエチレン−ビニルアルコール共重合体を備える多層結合体を問題なく同時延伸できるが、フィルムの酸素透過率値が不十分になる点が認められた。この試験での実際の延伸比は、機械方向に8〜1、横方向に5.5〜1であった。加熱区間では166℃及び178℃の間に温度を調整し、延伸区間では155℃と160℃との間に温度を調整し、二軸ポリプロピレンフィルムを製造する通常の温度条件と同一であった。165℃で最終的な熱定着を行なった。 In the case of a biaxial polypropylene film with the usual properties for co-stretching, within the scope of the work leading to the present invention, a multilayered composite comprising ethylene-vinyl alcohol copolymers with an ethylene concentration of 44 mol% and 48 mol% can be used without problems. Although it could be stretched simultaneously, it was found that the oxygen permeability value of the film was insufficient. The actual draw ratio in this test was 8 to 1 in the machine direction and 5.5 to 1 in the transverse direction. The temperature was adjusted between 166 ° C. and 178 ° C. in the heating section, and the temperature was adjusted between 155 ° C. and 160 ° C. in the stretching section, and the same temperature conditions as those for producing a biaxial polypropylene film were the same. Final heat fixing was performed at 165 ° C.
エチレン濃度44モル%及び48モル%のエチレン−ビニルアルコール共重合体を備える多層結合体は、高透明性で、不可視構造を示すが、臨界時の使用には酸素透過性が非常に強過ぎる。 Multi-layered conjugates comprising ethylene-vinyl alcohol copolymers with ethylene concentrations of 44 mol% and 48 mol% are highly transparent and exhibit an invisible structure, but are too oxygen permeable for critical use.
これに対して、従来の前記条件により製造される保護層でのエチレン濃度27〜38モル%のエチレン−ビニルアルコール共重合体を使用する多層結合は、二軸同時延伸試験で完全なエチレン−ビニルアルコール共重合体保護層の破壊を示す強い網目構造を有した。従って、従来の延伸条件の下では、品質の高い保護フィルムを製造することができない。 In contrast, a multi-layer bond using an ethylene-vinyl alcohol copolymer having an ethylene concentration of 27 to 38 mol% in a protective layer manufactured according to the above-described conventional conditions is completely ethylene-vinyl in a biaxial simultaneous stretching test. It had a strong network structure indicating destruction of the alcohol copolymer protective layer. Therefore, a high-quality protective film cannot be produced under conventional stretching conditions.
高品質の保護層に関して、最重要保護特性、機械的特性及び光学特性に関する以下のパラメータ範囲の分野における固有値の入手する試みがなされた。
フィルムの温度23℃で湿度75%の酸素透過性(OTR;ASTM-3985)を8cm3/(m2dbar)以下にすべきであり、エチレン−ビニルアルコール共重合体保護層の厚さを10μm未満にすべきである。合計ヤング熱膨張材料係数(Eモジュール、ASTM-D-822)は、長手方向及び横方向に2000N/mm2を越えるべきであり、引張強度(ASTM-D-822)は、長手方向及び横方向に300N/mm2を越えるべきである。光沢(ASTM-2457)を80以上にすべきであり、濁度(ASTM-1003)を5%以下とすべきである。また、フィルムに網目構造を形成してはならない。
For high-quality protective layers, attempts have been made to obtain eigenvalues in the field of the following parameter ranges for the most important protective properties, mechanical properties and optical properties.
Oxygen permeability (OTR; ASTM-3985) at a temperature of 23 ° C. and a humidity of 75% should be 8 cm 3 / (m 2 dbar) or less, and the thickness of the ethylene-vinyl alcohol copolymer protective layer is 10 μm. Should be less than. The total Young's coefficient of thermal expansion material (E module, ASTM-D-822) should exceed 2000 N / mm 2 in the longitudinal and transverse directions and the tensile strength (ASTM-D-822) should be in the longitudinal and transverse directions in should exceed 300N / mm 2. The gloss (ASTM-2457) should be above 80 and the turbidity (ASTM-1003) should be below 5%. In addition, a network structure should not be formed on the film.
発明者は、特に層Bの材料を適宜に選定し、145℃以下の温度で同時延伸を実施すれば、意外にも前記条件を備えるフィルムを製造できることを検証した。前記延伸条件の下で、必要なフィルム特性、特に8cm3/m2dbar以下の傑出する酸素透過率値を備える40モル%以下のエチレン濃度のエチレン−ビニルアルコール共重合体保護層を有する多層フィルムを得ることができる。エチレン−ビニルアルコール共重合体層の引裂現象(網目構造の形成)を阻止するため、50%/秒以上、好ましくは300%/秒以上の同時二軸延伸速度が適用される。 The inventor has verified that a film having the above conditions can be surprisingly produced by selecting the material of layer B appropriately and carrying out simultaneous stretching at a temperature of 145 ° C. or lower. A multilayer film having an ethylene-vinyl alcohol copolymer protective layer having an ethylene concentration of 40 mol% or less with the required film properties, particularly an outstanding oxygen permeability value of 8 cm 3 / m 2 dbar or less under the stretching conditions. Can be obtained. In order to prevent the tearing phenomenon (formation of a network structure) of the ethylene-vinyl alcohol copolymer layer, a simultaneous biaxial stretching speed of 50% / second or more, preferably 300% / second or more is applied.
特許文献6の方法より比較的低い温度での同時延伸を含む本発明による方法では、多層フィルムの全層を同じ幅で押出成形して、延伸の際に、全層を同時にクリップで把持する必要がなく、更に原則的に経済的に有利なフィルムの自由端への公知技術を適用できることも明らかである。また、64を越え又は46以下にもなる面積延伸比により、所望により大きなベルト幅を使用できることも明らかである。更に、被包装品に適合する収縮特性を備える収縮フィルムとしても保護フィルムを製造できる。 In the method according to the present invention including simultaneous stretching at a relatively lower temperature than the method of Patent Document 6, it is necessary to extrude all layers of a multilayer film with the same width, and to grip all the layers simultaneously with a clip during stretching. It is also clear that known techniques can be applied to the free end of the film, which is more economically advantageous in principle. It is also apparent that larger belt widths can be used if desired, with area stretch ratios exceeding 64 or even 46 or less. Further, the protective film can be manufactured as a shrink film having shrink characteristics suitable for a packaged product.
本発明を実施する温度145℃以下での延伸時に発生する位相変化及び結晶化過程の押圧によるエチレン−ビニルアルコール共重合体保護層内及び隣接する網目構造が形成されない延伸可能性を明確にできる。 The possibility of stretching in which the network structure in the ethylene-vinyl alcohol copolymer protective layer and the adjacent network structure are not formed due to the phase change that occurs when stretching at a temperature of 145 ° C. or less and the pressing of the crystallization process are carried out.
各構成層の例として、層A/層B/層C/層D/層C/層B/層Eについて、種々の適宜の構成をより詳細に以下説明する。 As examples of each constituent layer, various appropriate configurations of layer A / layer B / layer C / layer D / layer C / layer B / layer E will be described in more detail below.
エチレン−ビニルアルコール共重合体を含む保護内側層D:
エチレン−ビニルアルコール共重合体を含む内側層Dは、各層Dに関して少なくとも50重量%、好ましくは70〜100重量%、特に80〜100重量%の後述するエチレン−ビニルアルコール−共重合体(EVOH)を含む。
Protective inner layer D comprising ethylene-vinyl alcohol copolymer:
The inner layer D containing an ethylene-vinyl alcohol copolymer is at least 50% by weight, preferably 70-100% by weight, in particular 80-100% by weight of the ethylene-vinyl alcohol-copolymer (EVOH) described later, with respect to each layer D. including.
エチレン−ビニルアルコール共重合体は、従来公知であり、エチレン−ビニルアセテート−共重合体の鹸化又は加水分解により製造される。本発明の目的に対し、特に加水分解度96〜99%を有するエチレン−ビニルアルコール共重合体が適する。適宜のエチレン−ビニルアルコール共重合体の融点は、一般に150℃以上である。また、本発明では、エチレン−ビニルアルコール共重合体は、40モル%又はそれ以下のエチレン濃度を有し、エチレン−ビニルアルコール共重合体保護層の厚さは、通常1〜10μm、好ましくは1〜6μm、特に1〜3μmの範囲である。 The ethylene-vinyl alcohol copolymer is conventionally known and is produced by saponification or hydrolysis of an ethylene-vinyl acetate copolymer. For the purposes of the present invention, ethylene-vinyl alcohol copolymers having a degree of hydrolysis of 96-99% are particularly suitable. The melting point of an appropriate ethylene-vinyl alcohol copolymer is generally 150 ° C. or higher. In the present invention, the ethylene-vinyl alcohol copolymer has an ethylene concentration of 40 mol% or less, and the thickness of the ethylene-vinyl alcohol copolymer protective layer is usually 1 to 10 μm, preferably 1 It is in the range of ~ 6 μm, in particular 1 to 3 μm.
付着剤層C:
付着剤層Cを介してエチレン−ビニルアルコール共重合体保護層である内側層Dと構造層Bとを接着し結合することが必要である。従って、内側のエチレン−ビニルアルコール(EVOH)製の内側層Dと部分結晶性のポリオレフィンから成る構造層Bとの間に付着層が設けられる。付着層Cは、エチレン−ビニルアルコール共重合体の内側層Dと構造層Bとを互いに強固に接着して、付着層Cの両側に内側層Dと構造層Bとの付着を保持したまま、付着層Cと共に双方の内側層Dと構造層Bとを一体に延伸することができ、同時延伸装置で一体かつ同時に複数層に方向性を付与することができる。付着層Cは、変性ポリオレフィンをベースとする。
Adhesive layer C:
It is necessary to bond and bond the inner layer D, which is an ethylene-vinyl alcohol copolymer protective layer, and the structural layer B through the adhesive layer C. Therefore, an adhesion layer is provided between the inner layer D made of ethylene vinyl alcohol (EVOH) and the structural layer B made of partially crystalline polyolefin. The adhesion layer C firmly adheres the inner layer D and the structural layer B of the ethylene-vinyl alcohol copolymer to each other, and maintains adhesion between the inner layer D and the structural layer B on both sides of the adhesion layer C. Both the inner layer D and the structural layer B can be integrally stretched together with the adhesion layer C, and directivity can be imparted to a plurality of layers integrally and simultaneously with a simultaneous stretching device. The adhesion layer C is based on a modified polyolefin.
変性ポリオレフィンは、エチレン重合体又は特に好適なプロピレン重合体を基礎とし、プロピレン単独重合体、プロピレン共重合体又はプロピレン三量体である。プロピレン共重合体又はプロピレン三量体は、少なくとも80〜98重量%の圧倒的なプロピレンユニットと、コモノマーとして適宜量の追加エチレン及び/又はブチレンユニットとを含むとよい。無水マレイン酸、場合により他のカルボン酸モノマー又は例えばアクリル酸又は他の誘導体等の他のエステルによりこの重合体を変性するとよい。 The modified polyolefin is based on an ethylene polymer or a particularly suitable propylene polymer and is a propylene homopolymer, propylene copolymer or propylene trimer. The propylene copolymer or propylene trimer may contain at least 80 to 98% by weight of an overwhelming propylene unit and an appropriate amount of additional ethylene and / or butylene units as a comonomer. The polymer may be modified with maleic anhydride, optionally other carboxylic acid monomers or other esters such as acrylic acid or other derivatives.
変性ポリプロピレン及び変性ポリオレフィンは、公知であり、例えば三井ケミカル社製商品名Admer、又は三菱ケミカル社製商品名Modic、ケンプレックス(Chemplex)社製商品名Plexar、イーストマン(Eastman)社製商品名Epilene、デュポン(DuPont)社製商品名Bynelとして販売されている。 Modified polypropylene and modified polyolefin are known, for example, Miter Chemicals trade name Admer, Mitsubishi Chemicals trade name Modic, Chemplex trade name Plexar, Eastman trade name Epilene. It is sold under the trade name Bynel, manufactured by DuPont.
本発明の目的に対し、無水マレイン酸(例えば三井ケミカル社のQシリーズの製品)により変性され、230℃(ASTM-D-1238)の溶解物指数1〜10g/10分の範囲にあり、ビカット(Vicat)軟化点が110と155℃の間にあるプロピレン単独重合体又はプロピレン共重合体が好適である。 For the purposes of the present invention, it is modified with maleic anhydride (for example, Mitsui Chemicals Q series product) and has a melt index of 230 ° C. (ASTM-D-1238) in the range of 1-10 g / 10 min. (Vicat) A propylene homopolymer or propylene copolymer having a softening point between 110 and 155 ° C. is preferred.
付着層Cの厚さは、一般的にそれぞれ0.3〜5μm、好ましくは0.3〜3μm、特に0.3〜2μmである。 The thickness of the adhesion layer C is generally from 0.3 to 5 μm, preferably from 0.3 to 3 μm, in particular from 0.3 to 2 μm.
層B:
層Bは、二軸方向性付与可能なポリオレフィン、特にポリプロピレンから成る構造層であり、温度145℃以下での同時延伸の間付着を保持したまま、付着層Cに対し十分に大きな付着強度を発生すべきである。
Layer B:
Layer B is a structural layer made of polyolefin, particularly polypropylene, capable of imparting biaxiality, and generates sufficiently large adhesion strength to adhesion layer C while maintaining adhesion during simultaneous stretching at a temperature of 145 ° C. or lower. Should.
層Cの結晶度は、少なくとも10〜70%、好ましくは30〜70%であり、融点は、少なくとも110度である部分結晶性ポリオレフィンが適当である。 A partially crystalline polyolefin having a crystallinity of layer C of at least 10 to 70%, preferably 30 to 70% and a melting point of at least 110 degrees is suitable.
ポリオレフィンは、プロピレン重合体をベースとし、プロピレン単独重合体、プロピレン共重合体又はプロピレン三量体が好ましい。プロピレン共重合体又はプロピレン三量体は、少なくとも80〜98重量%の圧倒的なプロピレンユニットと、コモノマーとして適宜量の追加エチレン及び/又はブチレンユニットとを含むことが好ましい。 The polyolefin is based on a propylene polymer and is preferably a propylene homopolymer, a propylene copolymer or a propylene trimer. The propylene copolymer or propylene trimer preferably contains at least 80 to 98% by weight of an overwhelming propylene unit and an appropriate amount of additional ethylene and / or butylene units as a comonomer.
前記プロピレン重合体は、個別に使用し又は混合体として使用できる。また、145℃以下の延伸温度を許す変性を使用してもよい。例えば、アタクチックPP(ポリプロピレン)、シンジオタクチックPP、炭化水素樹脂、エチレン−プロピレン共重合体、プロピレン−ブチレン共重合体、エチレン−プロピレン−ブチレン−三量体、ポリブチレン、再生PP及び線形低密度ポリエチレン(PE-LLD)を変性体としてある範囲まで使用することが好ましい。 The propylene polymers can be used individually or as a mixture. Modifications that allow stretching temperatures of 145 ° C. or lower may also be used. For example, atactic PP (polypropylene), syndiotactic PP, hydrocarbon resin, ethylene-propylene copolymer, propylene-butylene copolymer, ethylene-propylene-butylene-trimer, polybutylene, recycled PP and linear low density polyethylene It is preferable to use (PE-LLD) as a modified substance to a certain extent.
全重合体に対し、エチレン濃度0〜15重量%間のプロピレン重合体を使用することが好ましい。特に、融点150〜170℃と、融液指数(21.6Nの負荷及び230℃での測定DIN53735)1.0〜15g/10分を有するアイソタクチックプロピレン重合体が適当である。プロピレン重合体の結晶度は、好ましくは40〜70%である。単独重合体の分子重量配分は、変更できる。数量平均Mnに対する重量平均Mwの比は、通常1と15との間である。 It is preferable to use a propylene polymer having an ethylene concentration of 0 to 15% by weight based on the total polymer. In particular, isotactic propylene polymers having a melting point of 150-170 ° C. and a melt index (measured DIN 53735 at 21.6 N load and 230 ° C.) of 1.0-15 g / 10 min are suitable. The crystallinity of the propylene polymer is preferably 40 to 70%. The molecular weight distribution of the homopolymer can be varied. The ratio of the weight average Mw to the quantity average Mn is usually between 1 and 15.
層Bの層厚は、3と35μmとの間、特に3〜15μmが好ましい。 The layer thickness of layer B is preferably between 3 and 35 μm, in particular 3 to 15 μm.
別の実施の形態では、層Bは、公知の不透明な二軸ポリプロピレンフィルムの不透明なベース層等の不透明な層でもよい。この実施の形態では、層Bは、充填材の添加により不透明となる。この実施の形態では、層Bは、層Bの重量に対し通常少なくとも70重量%の部分結晶性ポリオレフィンを含む。不透明な層B内の充填材濃度は、層Bの重量に対し10乃至50重量%の間であることが好ましい。本発明では、充填材は、色素及び/又は空隙を有する粒子でもあり、それ自体公知の材料である。 In another embodiment, layer B may be an opaque layer, such as an opaque base layer of a known opaque biaxial polypropylene film. In this embodiment, layer B becomes opaque due to the addition of filler. In this embodiment, layer B usually comprises at least 70% by weight of partially crystalline polyolefin, based on the weight of layer B. The filler concentration in the opaque layer B is preferably between 10 and 50% by weight with respect to the weight of the layer B. In the present invention, the filler is also a particle having a pigment and / or voids, and is a material known per se.
従来の色素及び/又は空隙を有する粒子は、例えば酸化アルミニウム、硫酸アルミニウム、硫酸バリウム、炭酸カルシウム、炭酸マグネシウム、ケイ酸アルミニウムやケイ酸マグネシウム等のケイ酸塩及び二酸化ケイ素等の無機粒子及び/又は有機粒子である。空隙を有する有機充填材としては、従来この目的に使用するベース層の重合体と相性の悪い重合体、特に、高密度ポリエチレン(HDPE)、エチレン又はプロペンを有するノルボルン又はテトラシクロドデカン等の環式オレフィンの共重合体、ポリエステル、ポリスチロール、ポリアミド、ハロゲン化有機重合体が問題になり、例えばポリブチレンテレフタレート等のポリエステルが好適である。 Conventional pigments and / or particles having voids include, for example, aluminum oxide, aluminum sulfate, barium sulfate, calcium carbonate, magnesium carbonate, silicates such as aluminum silicate and magnesium silicate, and inorganic particles such as silicon dioxide and / or Organic particles. As the organic filler having voids, polymers that are not compatible with the polymer of the base layer conventionally used for this purpose, in particular, high density polyethylene (HDPE), cyclic such as norborn or tetracyclododecane having ethylene or propene. Olefin copolymers, polyesters, polystyrene, polyamides, and halogenated organic polymers are problematic, and polyesters such as polybutylene terephthalate are preferred.
不透明な層Bの各構造に応じて、不透明な層B及びフィルムの密度を0.4〜1.1g/cm3の範囲で変更できる。 Depending on the structure of the opaque layer B, the density of the opaque layer B and the film can be varied in the range of 0.4 to 1.1 g / cm 3 .
カバー層A及びE
本発明によるフィルムは、付加的にエチレン−ビニルアルコール共重合体保護層D、二つの付着層C及びポリオレフィン層Bから成る構造に加えて、同一の又は異なる材質のカバー層により層Bの両表面を覆うことが好ましい。
Cover layers A and E
The film according to the invention additionally has a structure comprising an ethylene-vinyl alcohol copolymer protective layer D, two adhesion layers C and a polyolefin layer B, as well as both surfaces of layer B by means of a cover layer of the same or different material. It is preferable to cover.
このポリオレフィンカバー層は、完成する多層フィルム構造の外側に配置される層を構成し、追加の処理、印刷、被覆及び金属メッキ可能性等の特性によって、密封可能性、光沢、摩擦等の機能を決定する。 This polyolefin cover layer constitutes a layer that is placed outside the finished multilayer film structure and has functions such as sealability, gloss, friction, etc., due to additional processing, printing, coating and metal plating possibilities. decide.
カバー層に適するオレフィン重合体の例は、ポリエチレン、ポリプロピレン、ポリブチレン又は2個〜8個までの炭素原子を備えるオレフィンとの混合重合体、エチレン、プロピレン及び/又はブチレンユニットから成る共重合体、三量体又は前記重合体の混合体が好適である。 Examples of olefin polymers suitable for the cover layer are polyethylene, polypropylene, polybutylene or mixed polymers with olefins having from 2 to 8 carbon atoms, copolymers of ethylene, propylene and / or butylene units, three Preference is given to monomers or mixtures of said polymers.
各カバー層の厚さは、通常0.1μmより大きく、0.5〜10μmの範囲にあることが好ましい。 The thickness of each cover layer is preferably larger than 0.1 μm and preferably in the range of 0.5 to 10 μm.
カバー層及び/又は層Bは、付加的に、中和剤、安定剤、帯電防止剤、紫外線及び光保護剤、閉塞防止剤及び/又は潤滑剤等の公知の添加剤を各有効な量で含んでもよい。 The cover layer and / or layer B additionally contains known additives such as neutralizers, stabilizers, antistatic agents, ultraviolet and photoprotective agents, anti-clogging agents and / or lubricants in effective amounts. May be included.
コロナ、プラズマ又は炎熱処理をカバー層A及び/又はEの表面に施す実施の形態も本発明に含まれる。これらの処理は、公知の方法で、印刷インク、接着剤、常温封縅層、金属層等に対する付着性を向上する。 Embodiments in which corona, plasma or flame heat treatment is applied to the surface of the cover layers A and / or E are also included in the present invention. These treatments improve the adhesion to printing inks, adhesives, room temperature sealing layers, metal layers and the like by known methods.
意図する最終の使用目的により、本発明によるフィルムの全厚をより広い限界内で変更することができる。全厚は、好ましくは4〜100μm、特に5〜80μm、より好ましくは6〜60μmである。 Depending on the intended end use, the total thickness of the film according to the invention can be varied within wider limits. The total thickness is preferably 4 to 100 μm, in particular 5 to 80 μm, more preferably 6 to 60 μm.
当業者が本発明の方法条件、材料及びフィルム特性を実施し、他の目的及び利点を理解できるように、本発明の実施の形態を以下より詳細に説明する。 In order that those skilled in the art will be able to practice the method conditions, materials and film properties of the present invention and to understand other objects and advantages, embodiments of the present invention are described in more detail below.
例のうち、例1〜例17は、前記構造層A/層B/層C/層D/層C/層B/層Eのエチレン−ビニルアルコール共重合体層を有する全7層の多層フィルムの製造法を説明し、例1〜例6は、比較例である。 Among the examples, Examples 1 to 17 are a multilayer film having a total of 7 layers having the ethylene-vinyl alcohol copolymer layer of the structural layer A / layer B / layer C / layer D / layer C / layer B / layer E. The manufacturing method of Example 1 is demonstrated, and Examples 1-6 are comparative examples.
各例では、各処理名称を示す材料に下記種類の材料を使用した。
HP522H:バセル社製アイソタクチック構造ポリプロピレン単独重合体「Moplen(登録商標)」HP522H
HP422H:バセル社製アイソタクチック構造ポリプロピレン単独重合体「Moplen(登録商標)」HP422H(ミニランダム(Minirandom)エチレン濃度約1.5%)
「Admer(登録商標)」-QF551E:三井ケミカル社製無水変態ポリプロピレン樹脂
7372-XCP:バゼル社製ポリプロピレン三量体「Adsyl(登録商標)」7372-XCP
5C37-F:バゼル社製ポリプロピレン三量体「Adsyl(登録商標)」5C37F
MA-0935-PP:コンスタブ(Constab)社製50%炭化水素を含むポリプロピレンマスターバッチ(Masterbatch)
LC101-B:EVAL-EUROPE社製エチレン濃度27モル%を含むエチレン−ビニルアルコール−共重合体「EVAL(登録商標)」LC101B
F101-B:EVAL-EUROPE社製エチレン濃度32モル%を含むエチレン−ビニルアルコール−共重合体「EVAL(登録商標)」F101B
H101-B:EVAL-EUROPE社製エチレン濃度38モル%を含むエチレン−ビニルアルコール−共重合体「EVAL(登録商標)」H101B
ES104-B:EVAL-EUROPE社製エチレン濃度44モル%を含むエチレン−ビニルアルコール−共重合体「EVAL(登録商標)」ES104B
G156-B:EVAL-EUROPE社製エチレン濃度48モル%を含むエチレン−ビニルアルコール−共重合体「EVAL(登録商標)」G156B
SP482-B:EVAL-EUROPE社製エチレン濃度32モル%を含むエチレン−ビニルアルコール−共重合体「EVAL(登録商標)」SP482B
In each example, the following types of materials were used as materials indicating the treatment names.
HP522H: Isotactic structural polypropylene homopolymer "Moplen (registered trademark)" HP522H manufactured by Basel
HP422H: Isotactic polypropylene homopolymer “Moplen (registered trademark)” manufactured by Basel, Inc. HP422H (Minirandom ethylene concentration about 1.5%)
"Admer (registered trademark)"-QF551E: Anhydrous polypropylene resin manufactured by Mitsui Chemicals
7372-XCP: Basel polypropylene trimer "Adsyl (registered trademark)" 7372-XCP
5C37-F: Basel Polypropylene Trimer “Adsyl (registered trademark)” 5C37F
MA-0935-PP: Constab Polypropylene Masterbatch containing 50% hydrocarbon (Masterbatch)
LC101-B: EVAL-EUROPE manufactured ethylene-vinyl alcohol-copolymer “EVAL (registered trademark)” LC101B containing an ethylene concentration of 27 mol%
F101-B: an ethylene-vinyl alcohol-copolymer “EVAL (registered trademark)” F101B containing an ethylene concentration of 32 mol% manufactured by EVAL-EUROPE
H101-B: An ethylene-vinyl alcohol-copolymer “EVAL (registered trademark)” H101B containing an ethylene concentration of 38 mol% manufactured by EVAL-EUROPE
ES104-B: EVAL-EUROPE's ethylene-vinyl alcohol-copolymer “EVAL (registered trademark)” containing an ethylene concentration of 44 mol% ES104B
G156-B: An ethylene-vinyl alcohol-copolymer “EVAL (registered trademark)” G156B containing an ethylene concentration of 48 mol% manufactured by EVAL-EUROPE
SP482-B: EVAL-EUROPE's ethylene-vinyl alcohol-copolymer “EVAL (registered trademark)” SP482B containing an ethylene concentration of 32 mol%
[例]
[例1の前に]
例では、内側層としてエチレン−ビニルアルコール共重合体層を有する7層の保護多層フィルムを製造し、幅広スリット溶融物ノズルによる冷却ローラ上への7層押出成形を行ない、例示のように、ブリュックナー(Brueckner)社製Laboratoriums-LISIM(登録商標)延伸装置により、冷却ローラで形成した7層の初期フィルムを直ちに同時に延伸した。
[Example]
[ Before Example 1 ]
In the example, a 7-layer protective multilayer film having an ethylene-vinyl alcohol copolymer layer as an inner layer was produced, and 7-layer extrusion was performed on a cooling roller with a wide slit melt nozzle. A seven-layer initial film formed by a cooling roller was immediately and simultaneously stretched by a Laboratoriums-LISIM (registered trademark) stretching device manufactured by (Brueckner).
その際、多層フィルムを製造する溶融物の配置層A/層B/層C/層D/層C/層B/層Eは、所与の搬送装置から下記ノズル装置により形成される。
層A−外側層、空気ナイフ側:43mmの単軸スクリュー式押出成形機
層B−中間層:55mmの溶融物ポンプを備える2軸スクリュー式押出成形機
層C−付着層:35mmの溶融物ポンプを備える単軸スクリュー式押出成形機
層D−エチレン−ビニルアルコール共重合体芯層:35mmの溶融物ポンプを備える単軸スクリュー式押出成形機
層E−外側層、冷却ローラ側:50mmの単軸スクリュー式押出成形機
At that time, the arrangement layer A / layer B / layer C / layer D / layer C / layer B / layer E of the melt for producing the multilayer film is formed from a given conveying device by the following nozzle device.
Layer A—outer layer, air knife side: 43 mm single screw extruder Extrusion layer B—intermediate layer: twin screw extruder with 55 mm melt pump Layer C—adhesion layer: 35 mm melt pump Single screw extruder with layer D-ethylene-vinyl alcohol copolymer core layer: single screw extruder with 35 mm melt pump Layer E-outer layer, cooling roller side: 50 mm single shaft Screw extruder
冷却ローラ及び対向する空気ナイフに対する溶融物押出成形機の幅広スリットノズルの配置又は位置により、層A〜層Eの符号を付す点に注意すべきである。 It should be noted that layers A to E are labeled according to the placement or position of the wide slit nozzle of the melt extruder relative to the cooling roller and the opposing air knife.
比較例を示す例1〜例6では、二軸方向性ポリプロピレンフィルム(s-BOPPフィルム)の同時方向性付与に最適化する条件下で、内側層としてエチレン−ビニルアルコール共重合体層を備える7層の保護多層フィルムに方向性が付与される。最適化する条件は、良好な厚さ許容誤差及び経済的な製造を確立するのに必要な動作安全性に対して、所望の機械的特性と光学特性との組合せ特性を有する二軸ポリプロピレンフィルムを供給する。標準ポリプロピレン単独重合体を使用する延伸温度は、150〜160℃の範囲、好ましくは155℃である。 In Examples 1 to 6, which show comparative examples, an ethylene-vinyl alcohol copolymer layer is provided as an inner layer under conditions optimized for imparting simultaneous directionality of a biaxially oriented polypropylene film (s-BOPP film). Directionality is imparted to the protective multilayer film of the layer. The conditions to be optimized are biaxial polypropylene films with the desired combination of mechanical and optical properties for good thickness tolerances and the operational safety necessary to establish economical manufacturing. Supply. The stretching temperature using standard polypropylene homopolymer is in the range of 150-160 ° C, preferably 155 ° C.
本発明による例7〜例17では、内側層としてエチレン−ビニルアルコール共重合体層を有する7層の保護多層フィルムは、温度145℃以下、特に140℃以下、好ましくはほぼ135℃で延伸される。その際、延伸温度を低下するため、層Bを使用しかつ例7〜例17に示す材料を使用して達成できる層Bの変性が必要である。 In Examples 7 to 17 according to the present invention, a seven-layer protective multilayer film having an ethylene-vinyl alcohol copolymer layer as an inner layer is stretched at a temperature of 145 ° C. or lower, particularly 140 ° C. or lower, preferably approximately 135 ° C. . In so doing, in order to lower the stretching temperature, a modification of layer B is required which can be achieved using layer B and using the materials shown in examples 7-17.
[例1](比較例)
材料及び5つの押出成形機の運転条件は、以下の通りである。
層A:5C37-F、抽出温度240℃の押出成形機
層B:HP-522H、抽出温度258℃の押出成形機
層C:Admer-QF551E、抽出温度236℃の押出成形機
層D:G156-B、抽出温度186℃の押出成形機
層E:5C37-F、抽出温度240℃の押出成形機
[ Example 1 ] (Comparative example)
The operating conditions of the material and the five extruders are as follows.
Layer A: Extruder with 5C37-F, extraction temperature 240 ° C Layer B: Extruder with HP-522H, extraction temperature 258 ° C Layer C: Extruder with Admer-QF551E, extraction temperature 236 ° C Layer D: G156- B, Extruder with extraction temperature of 186 ° C Layer E: 5C37-F, Extruder with extraction temperature of 240 ° C
7層溶融物の同時押出成形により得られる初期フィルムは、二軸方向性ポリプロピレンフィルム(S-BOPPフィルム)の同時方向性付与に最適化される条件の下で、ベースフィルム上で延伸前に印刷される格子の拡大比により、機械方向(MD)に7倍延伸及び横方向(TD)に6倍延伸をもって方向性を付与した。延伸区間の延伸温度は、158℃であった。弛緩率は、長手方向に5%、横方向に5%であった。全厚20μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.4mであった。得られたフィルムの外観は、輝きを有し、いかなる網目構造も認められなかった。引張強度は、長手方向に241N/mm2、横方向に187N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2471N/mm2、横方向に1929N/mm2であった。破断点伸び率は、長手方向に93%、横方向に143%であった。濁度値は、1.0%であった。光沢は、91であった。120℃で5分間の収縮率は、長手方向に4.1%、横方向に3.1%であった。しかしながら、酸素遮断性は、僅か81.2cm3/m2dbarであった。 The initial film obtained by co-extrusion of the 7-layer melt is printed before stretching on the base film under conditions optimized for the simultaneous orientation of biaxially oriented polypropylene film (S-BOPP film). Depending on the enlargement ratio of the lattice, directionality was imparted by stretching 7 times in the machine direction (MD) and stretching 6 times in the transverse direction (TD). The stretching temperature in the stretching section was 158 ° C. The relaxation rate was 5% in the longitudinal direction and 5% in the lateral direction. A film having a total thickness of 20 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (Layer D) was approximately 1.4 m. The appearance of the film obtained was brilliant and no network structure was observed. Tensile strength, longitudinal direction 241n / mm 2, in the transverse direction was 187N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2471N / mm 2, in the transverse direction was 1929N / mm 2. The elongation at break was 93% in the longitudinal direction and 143% in the lateral direction. The turbidity value was 1.0%. The gloss was 91. The shrinkage rate at 120 ° C. for 5 minutes was 4.1% in the longitudinal direction and 3.1% in the lateral direction. However, the oxygen barrier was only 81.2 cm 3 / m 2 dbar.
[例2](比較例)
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度44モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-ES104-Bを層Dに使用した。抽出温度は、223℃であった。延伸区間の延伸温度は、156.5℃であった。全厚20μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.8μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造も認められなかった。引張強度は、長手方向に238N/mm2、横方向に193N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2480N/mm2、横方向に2090N/mm2であった。破断点伸び率は、長手方向に95%、横方向に134%であった。濁度値は、0.95%であった。光沢は、91であった。120℃で5分間の収縮率は、長手方向に4.3%、横方向に4.1%であった。しかしながら、酸素遮断性は、僅か62.7cm3/m2dbarであった。
[ Example 2 ] (Comparative example)
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-ES104-B having an ethylene concentration of 44 mol% and 100 wt% was used for layer D. The extraction temperature was 223 ° C. The stretching temperature in the stretching section was 156.5 ° C. A film having a total thickness of 20 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.8 μm. The appearance of the resulting film was brilliant and no network structure was observed. Tensile strength, longitudinal direction 238N / mm 2, in the transverse direction was 193N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2480N / mm 2, in the transverse direction was 2090N / mm 2. The elongation at break was 95% in the longitudinal direction and 134% in the lateral direction. The turbidity value was 0.95%. The gloss was 91. The shrinkage rate at 120 ° C. for 5 minutes was 4.3% in the longitudinal direction and 4.1% in the lateral direction. However, the oxygen barrier was only 62.7 cm 3 / m 2 dbar.
[例3](比較例)
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度38モル%の100重量%のエチレン−ビニルアルコール−共重合体EVAL-H101-Bを層Dに使用した。抽出温度は、208℃であった。延伸区間の延伸温度は、155.5℃であった。延伸比は、機械方向に7、横方向に6.5であった。全厚20μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.7μmであった。得られたフィルムは、濁る外観と、強い網目構造を有した。
[ Example 3 ] (Comparative example)
A film was prepared as in Example 1. Unlike Example 1, 100% by weight ethylene-vinyl alcohol-copolymer EVAL-H101-B with an ethylene concentration of 38 mol% was used for layer D. The extraction temperature was 208 ° C. The stretching temperature in the stretching section was 155.5 ° C. The draw ratio was 7 in the machine direction and 6.5 in the transverse direction. A film having a total thickness of 20 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (Layer D) was approximately 1.7 μm. The resulting film had a cloudy appearance and a strong network structure.
[例4](比較例)
例1と同様の方法で、フィルムを製造した。例1とは異なり、エチレン濃度32モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-F101-Bを層Dに使用した。抽出温度は、208℃であった。延伸区間の延伸温度は、158.5℃であった。延伸比は、機械方向に7、横方向に6であった。全厚20μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.7μmであった。得られたフィルムは、濁る外観と、強い網目構造を有した。
[ Example 4 ] (Comparative example)
A film was produced in the same manner as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-F101-B having an ethylene concentration of 32 mol% and 100 wt% was used for layer D. The extraction temperature was 208 ° C. The stretching temperature in the stretching section was 158.5 ° C. The draw ratio was 7 in the machine direction and 6 in the transverse direction. A film having a total thickness of 20 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (Layer D) was approximately 1.7 μm. The resulting film had a cloudy appearance and a strong network structure.
[例5](比較例)
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度27モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-LC101-Bを層Dに使用した。抽出温度は、207℃であった。延伸区間の延伸温度は、156.5℃であった。延伸比は、機械方向に7、横方向に6.7であった。全厚18μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.1μmであった。得られたフィルムの外観は、濁り、強い網目構造が認められた。
[ Example 5 ] (Comparative example)
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-LC101-B having an ethylene concentration of 27 mol% and 100 wt% was used for layer D. The extraction temperature was 207 ° C. The stretching temperature in the stretching section was 156.5 ° C. The draw ratio was 7 in the machine direction and 6.7 in the transverse direction. A film having a total thickness of 18 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.1 μm. The appearance of the obtained film was cloudy and a strong network structure was observed.
[例6](比較例)
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度32モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-SP482-Bを層Dに使用した。この新規EVAL型は、対応する保護の際に改良された光学特性を保証すべきである。抽出温度は、207℃であった。延伸区間の延伸温度は、157.5℃であった。延伸比は、機械方向に7、横方向に6.2であった。全厚15.5μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.2μmであった。得られたフィルムの外観は、少し濁りがあった。フィルム上に小さな斑点があったが、網目構造は、認められなかった。しかしながら、酸素遮断性は、僅か185cm3/m2dbarであった。
[ Example 6 ] (Comparative example)
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-SP482-B having an ethylene concentration of 32 mol% and 100 wt% was used for layer D. This new EVAL type should guarantee improved optical properties during corresponding protection. The extraction temperature was 207 ° C. The stretching temperature in the stretching section was 157.5 ° C. The draw ratio was 7 in the machine direction and 6.2 in the transverse direction. A film having a total thickness of 15.5 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.2 μm. The appearance of the obtained film was slightly turbid. There were small spots on the film, but no network structure was observed. However, the oxygen barrier was only 185 cm 3 / m 2 dbar.
[例7]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度38モル%の100重量%のエチレン−ビニルアルコール−共重合体EVAL-H101-Bを層Dに使用した。抽出温度は、226℃であった。ポリプロピレン単独重合体(HP522-H)50重量%と、ポリプロピレン三量体(7372-XCP)50重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を137.5℃に低下できた。延伸比は、機械方向に6、横方向に5.8であった。全厚19μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.7μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に210N/mm2、横方向に179N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に1830N/mm2、横方向に1638N/mm2であった。破断点伸び率は、長手方向に84%、横方向に93%であった。濁度値は、1.8%であった。光沢は、89であった。120℃で5分間の収縮率は、長手方向に13.2%、横方向に14.1%であった。酸素遮断性は、6.2cm3/m2dbarであった。
[ Example 7 ]
A film was prepared as in Example 1. Unlike Example 1, 100% by weight ethylene-vinyl alcohol-copolymer EVAL-H101-B with an ethylene concentration of 38 mol% was used for layer D. The extraction temperature was 226 ° C. A mixture of 50% by weight of polypropylene homopolymer (HP522-H) and 50% by weight of polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 137.5 degreeC. The draw ratio was 6 in the machine direction and 5.8 in the transverse direction. A film having a total thickness of 19 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.7 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 210N / mm 2, in the transverse direction was 179N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 1830N / mm 2, in the transverse direction was 1638N / mm 2. The elongation at break was 84% in the longitudinal direction and 93% in the lateral direction. The turbidity value was 1.8%. The gloss was 89. The shrinkage ratio at 120 ° C. for 5 minutes was 13.2% in the longitudinal direction and 14.1% in the lateral direction. The oxygen barrier property was 6.2 cm 3 / m 2 dbar.
[例8]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度32モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-F101-Bを層Dに使用した。抽出温度は、218℃であった。
ポリプロピレン単独重合体(HP522-H)50重量%と、ポリプロピレン三量体(7372-XCP)50重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を137℃に低下できた。延伸比は、機械方向に6、横方向に6であった。全厚19μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.4μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に181N/mm2、横方向に204N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に1591N/mm2、横方向に1739N/mm2であった。破断点伸び率は、長手方向に87%、横方向に77%であった。濁度値は、2.0%であった。光沢は、89であった。120℃で5分間の収縮率は、長手方向に14.1%、横方向に15.5%であった。酸素遮断性は、3.0cm3/m2dbarであった。
[ Example 8 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-F101-B having an ethylene concentration of 32 mol% and 100 wt% was used for layer D. The extraction temperature was 218 ° C.
A mixture of 50% by weight of polypropylene homopolymer (HP522-H) and 50% by weight of polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area could be reduced to 137 degreeC. The draw ratio was 6 in the machine direction and 6 in the transverse direction. A film having a total thickness of 19 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (Layer D) was approximately 1.4 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 181N / mm 2, in the transverse direction was 204N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 1591N / mm 2, in the transverse direction was 1739N / mm 2. The elongation at break was 87% in the longitudinal direction and 77% in the lateral direction. The turbidity value was 2.0%. The gloss was 89. The shrinkage ratio at 120 ° C. for 5 minutes was 14.1% in the longitudinal direction and 15.5% in the lateral direction. The oxygen barrier property was 3.0 cm 3 / m 2 dbar.
[例9]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度32モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-F101-Bを層Dに使用した。抽出温度は、218℃であった。ポリプロピレン単独重合体(HP522-H)60重量%と、ポリプロピレン三量体(7372-XCP)40重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を138.5℃に低下できた。延伸比は、機械方向に7、横方向に5.8であった。全厚16.5μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.3μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に253N/mm2、横方向に170N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2408N/mm2、横方向に1772N/mm2であった。破断点伸び率は、長手方向に62%、横方向に98%であった。濁度値は、2.1%であった。光沢は、88であった。120℃で5分間の収縮率は、長手方向に14.0%、横方向に11.1%であった。酸素遮断性は、3.0cm3/m2dbarであった。
[ Example 9 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-F101-B having an ethylene concentration of 32 mol% and 100 wt% was used for layer D. The extraction temperature was 218 ° C. A mixture of 60% by weight polypropylene homopolymer (HP522-H) and 40% by weight polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 138.5 degreeC. The draw ratio was 7 in the machine direction and 5.8 in the transverse direction. A film having a total thickness of 16.5 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.3 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 253N / mm 2, in the transverse direction was 170N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2408N / mm 2, in the transverse direction was 1772N / mm 2. The elongation at break was 62% in the longitudinal direction and 98% in the transverse direction. The turbidity value was 2.1%. The gloss was 88. The shrinkage rate at 120 ° C. for 5 minutes was 14.0% in the longitudinal direction and 11.1% in the lateral direction. The oxygen barrier property was 3.0 cm 3 / m 2 dbar.
[例10]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度32モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-F101-Bを層Dに使用した。抽出温度は、218℃であった。ポリプロピレン単独重合体(HP522-H)60重量%と、ポリプロピレン三量体(7372-XCP)40重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を137.5℃に低下できた。延伸比は、機械方向に6、横方向に5.8であった。全厚20μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.6μmであった。弛緩率は、長手方向に15%、横方向に15%であった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に217N/mm2、横方向に156N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に1929N/mm2、横方向に1572N/mm2であった。破断点伸び率は、長手方向に82%、横方向に116%であった。濁度値は、2.2%であった。光沢は、85であった。120℃で5分間の収縮率は、長手方向に5.1%、横方向に4.8%であった。酸素遮断性は、3.3cm3/m2dbarであった。
[ Example 10 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-F101-B having an ethylene concentration of 32 mol% and 100 wt% was used for layer D. The extraction temperature was 218 ° C. A mixture of 60% by weight polypropylene homopolymer (HP522-H) and 40% by weight polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 137.5 degreeC. The draw ratio was 6 in the machine direction and 5.8 in the transverse direction. A film having a total thickness of 20 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.6 μm. The relaxation rate was 15% in the longitudinal direction and 15% in the lateral direction. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 217N / mm 2, in the transverse direction was 156N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 1929N / mm 2, in the transverse direction was 1572N / mm 2. The elongation at break was 82% in the longitudinal direction and 116% in the lateral direction. The turbidity value was 2.2%. The gloss was 85. The shrinkage rate at 120 ° C. for 5 minutes was 5.1% in the longitudinal direction and 4.8% in the lateral direction. The oxygen barrier property was 3.3 cm 3 / m 2 dbar.
[例11]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度32モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-F101-Bを層Dに使用した。抽出温度は、218℃であった。ポリプロピレン単独重合体(HP522-H)80重量%と、ポリプロピレン三量体(7372-XCP)20重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を135.0℃に低下できた。延伸比は、機械方向に7、横方向に5.8であった。全厚17μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.4μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に269N/mm2、横方向に187N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2618N/mm2、横方向に2063N/mm2であった。破断点伸び率は、長手方向に65%、横方向に87%であった。濁度値は、2.2%であった。光沢は、83であった。120℃で5分間の収縮率は、長手方向に14.0%、横方向に10.2%であった。酸素遮断性は、3.0cm3/m2dbarであった。
[ Example 11 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-F101-B having an ethylene concentration of 32 mol% and 100 wt% was used for layer D. The extraction temperature was 218 ° C. A mixture of 80% by weight polypropylene homopolymer (HP522-H) and 20% by weight polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 135.0 degreeC. The draw ratio was 7 in the machine direction and 5.8 in the transverse direction. A film having a total thickness of 17 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.4 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 269N / mm 2, in the transverse direction was 187N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2618N / mm 2, in the transverse direction was 2063N / mm 2. The elongation at break was 65% in the longitudinal direction and 87% in the transverse direction. The turbidity value was 2.2%. The gloss was 83. The shrinkage ratio at 120 ° C. for 5 minutes was 14.0% in the longitudinal direction and 10.2% in the lateral direction. The oxygen barrier property was 3.0 cm 3 / m 2 dbar.
[例12]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度27モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-LC101-Bを層Dに使用した。抽出温度は、217℃であった。ポリプロピレン単独重合体(HP522-H)80重量%と、ポリプロピレン三量体(7372-XCP)20重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を136.0℃に低下できた。延伸比は、機械方向に7、横方向に5.8であった。全厚16.4μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.4μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に260N/mm2、横方向に189N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2547N/mm2、横方向に2092N/mm2であった。破断点伸び率は、長手方向に64%、横方向に85%であった。濁度値は、1.7%であった。光沢は、88であった。120℃で5分間の収縮率は、長手方向に11.6%、横方向に9.6%であった。酸素遮断性は、2.3cm3/m2dbarであった。
[ Example 12 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-LC101-B having an ethylene concentration of 27 mol% and 100 wt% was used for layer D. The extraction temperature was 217 ° C. A mixture of 80% by weight polypropylene homopolymer (HP522-H) and 20% by weight polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 136.0 degreeC. The draw ratio was 7 in the machine direction and 5.8 in the transverse direction. A film having a total thickness of 16.4 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.4 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 260 N / mm 2, in the transverse direction was 189N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2547N / mm 2, in the transverse direction was 2092N / mm 2. The elongation at break was 64% in the longitudinal direction and 85% in the transverse direction. The turbidity value was 1.7%. The gloss was 88. The shrinkage ratio at 120 ° C. for 5 minutes was 11.6% in the longitudinal direction and 9.6% in the lateral direction. The oxygen barrier property was 2.3 cm 3 / m 2 dbar.
[例13]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度27モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-LC101-Bを層Dに使用した。抽出温度は217℃であった。ポリプロピレン単独重合体(HP522-H)80重量%と、ポリプロピレン三量体(7372-XCP)20重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を136.0℃に低下できた。延伸比は、機械方向に6.3、横方向に5.2であった。弛緩率は、長手方向に15%、横方向に15%であった。全厚21.0μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.7μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に225N/mm2、横方向に159N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2133N/mm2、横方向に1868N/mm2であった。破断点伸び率は、長手方向に85%、横方向に97%であった。濁度値は、1.6%であった。光沢は、89であった。120℃で5分間の収縮率は、長手方向に3.0%、横方向に3.1%であった。酸素遮断性は、2.0cm3/m2dbarであった。
[ Example 13 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-LC101-B having an ethylene concentration of 27 mol% and 100 wt% was used for layer D. The extraction temperature was 217 ° C. A mixture of 80% by weight polypropylene homopolymer (HP522-H) and 20% by weight polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 136.0 degreeC. The draw ratio was 6.3 in the machine direction and 5.2 in the transverse direction. The relaxation rate was 15% in the longitudinal direction and 15% in the lateral direction. A film having a total thickness of 21.0 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.7 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 225N / mm 2, in the transverse direction was 159N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2133N / mm 2, in the transverse direction was 1868N / mm 2. The elongation at break was 85% in the longitudinal direction and 97% in the lateral direction. The turbidity value was 1.6%. The gloss was 89. The shrinkage rate at 120 ° C. for 5 minutes was 3.0% in the longitudinal direction and 3.1% in the lateral direction. The oxygen barrier property was 2.0 cm 3 / m 2 dbar.
[例14]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度32モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-F101-Bを層Dに使用した。抽出温度は、217℃であった。ポリプロピレン単独重合体(HP522-H)80重量%と、ポリプロピレン三量体(7372-XCP)20重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を136.5℃に低下できた。延伸比は、機械方向に6、横方向に5.3であった。弛緩率は、長手方向に15%、横方向に15%であった。全厚20.0μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.7μmであった。得られたフィルムは、輝きのある外観であって、いかなる網目構造もなかった。引張強度は、長手方向に231N/mm2、横方向に168N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2118N/mm2、横方向に1807N/mm2であった。破断点伸び率は、長手方向に88%、横方向に107%であった。濁度値は、1.5%であった。光沢は、89であった。120℃で5分間の収縮率は、長手方向に3.3%、横方向に1.9%であった。酸素遮断性は、2.8cm3/m2dbarであった。
[ Example 14 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-F101-B having an ethylene concentration of 32 mol% and 100 wt% was used for layer D. The extraction temperature was 217 ° C. A mixture of 80% by weight polypropylene homopolymer (HP522-H) and 20% by weight polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 136.5 degreeC. The draw ratio was 6 in the machine direction and 5.3 in the transverse direction. The relaxation rate was 15% in the longitudinal direction and 15% in the lateral direction. A film having a total thickness of 20.0 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.7 μm. The resulting film had a lustrous appearance and did not have any network structure. Tensile strength, longitudinal direction 231N / mm 2, in the transverse direction was 168N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2118N / mm 2, in the transverse direction was 1807N / mm 2. The elongation at break was 88% in the longitudinal direction and 107% in the lateral direction. The turbidity value was 1.5%. The gloss was 89. The shrinkage rate at 120 ° C. for 5 minutes was 3.3% in the longitudinal direction and 1.9% in the lateral direction. The oxygen barrier property was 2.8 cm 3 / m 2 dbar.
[例15]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度38モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-H101-Bを層Dに使用した。抽出温度は、218℃であった。ポリプロピレン単独重合体(HP522-H)80重量%と、ポリプロピレン三量体(7372-XCP)20重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を136.0℃に低下できた。延伸比は、機械方向に7、横方向に6であった。全厚16.0μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.3μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に264N/mm2、横方向に200N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2526N/mm2、横方向に1998N/mm2であった。破断点伸び率は、長手方向に73%、横方向に99%であった。濁度値は、1.4%であった。光沢は、90であった。120℃で5分間の収縮率は、長手方向に9.9%、横方向に8%であった。酸素遮断性は、8.2cm3/m2dbarであった。
[ Example 15 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-H101-B having an ethylene concentration of 38 mol% and 100 wt% was used for layer D. The extraction temperature was 218 ° C. A mixture of 80% by weight polypropylene homopolymer (HP522-H) and 20% by weight polypropylene trimer (7372-XCP) was used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 136.0 degreeC. The draw ratio was 7 in the machine direction and 6 in the transverse direction. A film having a total thickness of 16.0 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.3 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 264N / mm 2, in the transverse direction was 200 N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2526N / mm 2, in the transverse direction was 1998N / mm 2. The elongation at break was 73% in the longitudinal direction and 99% in the transverse direction. The turbidity value was 1.4%. The gloss was 90. The shrinkage ratio at 120 ° C. for 5 minutes was 9.9% in the longitudinal direction and 8% in the lateral direction. The oxygen barrier property was 8.2 cm 3 / m 2 dbar.
[例16]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度27モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-LC101-Bを層Dに使用した。抽出温度は218℃であった。エチレン濃度1.5%のポリプロピレンミニランダム(Minirandom)(HP422-H)100重量%を層Bに使用した。これにより、延伸区間での延伸温度を135℃に低下できた。延伸比は、機械方向に6、横方向に6であった。全厚17.0μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.5μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に224N/mm2、横方向に210N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2376N/mm2、横方向に2376N/mm2であった。破断点伸び率は、長手方向に76%、横方向に75%であった。濁度値は、0.95%であった。光沢は、91であった。120℃で5分間の収縮率は、長手方向に7.6%、横方向に7.4%であった。酸素遮断性は、1.8cm3/m2dbarであった。
[ Example 16 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-LC101-B having an ethylene concentration of 27 mol% and 100 wt% was used for layer D. The extraction temperature was 218 ° C. 100% by weight of polypropylene minirandom (HP422-H) with an ethylene concentration of 1.5% was used for layer B. Thereby, the extending | stretching temperature in an extending | stretching area was able to be reduced to 135 degreeC. The draw ratio was 6 in the machine direction and 6 in the transverse direction. A film having a total thickness of 17.0 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.5 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 224N / mm 2, in the transverse direction was 210N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2376N / mm 2, in the transverse direction was 2376N / mm 2. The elongation at break was 76% in the longitudinal direction and 75% in the lateral direction. The turbidity value was 0.95%. The gloss was 91. The shrinkage ratio at 120 ° C. for 5 minutes was 7.6% in the longitudinal direction and 7.4% in the lateral direction. The oxygen barrier property was 1.8 cm 3 / m 2 dbar.
[例17]
例1と同様に、フィルムを製造した。例1とは異なり、エチレン濃度27モル%、100重量%のエチレン−ビニルアルコール−共重合体EVAL-LC101-Bを層Dに使用した。抽出温度は、218℃であった。エチレン濃度1.5%のポリプロピレンミニランダム(Minirandom)(HP422-H)90重量%と、炭化水素50%を有するポリプロピレンマスターバッチ(Masterbatch)(MA-0935-PP)10重量%との混合体を層Bに使用した。これにより、延伸区間の延伸温度を135.0℃に低下できた。延伸比は、機械方向に6、横方向に6.2であった。全厚17.5μmのフィルムが得られ、エチレン−ビニルアルコール共重合体層(層D)の厚さは、ほぼ1.5μmであった。得られたフィルムの外観は、輝きがあり、いかなる網目構造もなかった。引張強度は、長手方向に231N/mm2、横方向に195N/mm2であった。ヤング熱膨張材料係数(Eモジュール)は、長手方向に2807N/mm2、横方向に2626N/mm2であった。破断点伸び率は、長手方向に77%、横方向に77%であった。濁度値は、0.93%であった。光沢は、92であった。収縮率は、120℃で5分間において、長手方向に7.2%、横方向に6.8%であった。酸素遮断性は、1.7cm3/m2dbarであった。
[ Example 17 ]
A film was prepared as in Example 1. Unlike Example 1, an ethylene-vinyl alcohol-copolymer EVAL-LC101-B having an ethylene concentration of 27 mol% and 100 wt% was used for layer D. The extraction temperature was 218 ° C. A mixture of 90% polypropylene minirandom (HP422-H) with 1.5% ethylene concentration and 10% polypropylene masterbatch (MA-0935-PP) with 50% hydrocarbons. Used for layer B. Thereby, the extending | stretching temperature of the extending | stretching area was able to be reduced to 135.0 degreeC. The draw ratio was 6 in the machine direction and 6.2 in the transverse direction. A film having a total thickness of 17.5 μm was obtained, and the thickness of the ethylene-vinyl alcohol copolymer layer (layer D) was approximately 1.5 μm. The appearance of the resulting film was brilliant and did not have any network structure. Tensile strength, longitudinal direction 231N / mm 2, in the transverse direction was 195 N / mm 2. Young thermal expansion material coefficient (E module) in the longitudinal direction 2807N / mm 2, in the transverse direction was 2626N / mm 2. The elongation at break was 77% in the longitudinal direction and 77% in the transverse direction. The turbidity value was 0.93%. The gloss was 92. The shrinkage was 7.2% in the longitudinal direction and 6.8% in the lateral direction at 120 ° C. for 5 minutes. The oxygen barrier property was 1.7 cm 3 / m 2 dbar.
[結果]
前記例に記載したフィルム製造試験の結果は、本発明により、傑出する保護特性と、更に際立ちかつ包装目的に望ましい組合せ特性とを備えるエチレン−ビニルアルコール共重合体保護層を有する二軸ポリプロピレンフィルムが得られる点、芳香及び臭気密閉性に関する傑出する特性及び傑出する他の保護特性に加えて、非常に良好なフィルム強度、剛性、傑出する光学特性が得られる点を明示する。保護特性を収縮特性に結合することもできる。
[ Result ]
The results of the film production test described in the above examples show that, according to the present invention, a biaxial polypropylene film having an ethylene-vinyl alcohol copolymer protective layer with outstanding protective properties and more prominent and desirable combination properties for packaging purposes. In addition to the points obtained, outstanding properties relating to fragrance and odor sealing and other outstanding protective properties, it is demonstrated that very good film strength, rigidity and outstanding optical properties are obtained. It is also possible to combine the protective property with the shrinkage property.
前記例に示す製造条件の範囲は、実験中に使用できる設備により制限されるが、所与の具体的な方法条件は、本発明又は本発明によるフィルム製造方法の限界を表わすものではない。意図するフィルムの使用に依存して、例えば、特に必要であれば、10μmまでの保護層の厚さを得ることができる。 The range of production conditions shown in the above examples is limited by the equipment that can be used during the experiment, but the given specific process conditions do not represent the limits of the present invention or the film production process according to the present invention. Depending on the intended use of the film, protective layer thicknesses of up to 10 μm can be obtained, for example, if necessary.
また、同時延伸の条件を制御して、得られるフィルムを安定化できるので、製造時の機械方向(MD)又は横方向(TD)に対応する主方向の一方又は双方に5%以下の収縮率を得ることができる点を指摘できる。しかしながら、120℃での一方向又は双方向の収縮率を15%以上となる延伸条件を選定してもよい。 In addition, since the film obtained can be stabilized by controlling the conditions of simultaneous stretching, the shrinkage rate is 5% or less in one or both of the main directions corresponding to the machine direction (MD) or the transverse direction (TD) during production. It can be pointed out that can be obtained. However, it is possible to select a stretching condition that makes the unidirectional or bidirectional shrinkage at 120 ° C. 15% or more.
更に、7層構造では、ポリプロピレン再生品を使用し又は他方の層Bに使用するポリプロピレンとは異なるポリオレフィンを使用しても、使用する最終用途に従って、一方のポリプロピレン層Bを製造できる点を指摘できる。 Furthermore, it can be pointed out that in the seven-layer structure, one polypropylene layer B can be produced according to the end use to be used, even if a recycled polypropylene product or a polyolefin different from the polypropylene used for the other layer B is used. .
傑出する保護特性に基づき、本発明のフィルムは、包装する商品が芳香損失を受けずかつ/又は包装を通して臭気拡散の生じない全包装目的に適する。本発明によるフィルムの僅かな酸素透過性及び僅かな蒸気透過性は、現在より高価なポリビニルアルコール(PVOH)又はポリ塩化ビニリデン(PVDC)により被覆された二軸ポリプロピレンフィルムを使用すべき最多使用に適する。 Based on outstanding protective properties, the film of the present invention is suitable for all packaging purposes in which the packaged goods are not subject to fragrance loss and / or odor diffusion does not occur through the packaging. The slight oxygen permeability and the slight vapor permeability of the film according to the invention are suitable for the most frequent use of biaxial polypropylene films coated with polyvinyl alcohol (PVOH) or polyvinylidene chloride (PVDC), which are more expensive than the present .
特に好適な使用方法は、食料品、例えば新鮮な食料品、菓子類及びケーキの包装への使用である。例えば薬品等他の商品の包装にもフィルムを使用できる。良好な光学特性に基づき、消費者が透明な保護材料を期待する全ての場合に、フィルムを使用できる。 A particularly preferred method of use is for the packaging of foodstuffs such as fresh foodstuffs, confectionery and cakes. For example, films can be used for packaging other products such as medicines. Based on good optical properties, the film can be used in all cases where consumers expect a transparent protective material.
Claims (21)
同時押出成形された多層初期フィルムの同時延伸により製造され、少なくとも厚さ5μm以下のエチレン−ビニルアルコール共重合体層を有し、温度23℃、相対湿度75%での酸素透過率(OTR;ASTM-3985)は、10cm3/m2dbar未満であり、
層B/層C/層D/層C/層Bの少なくとも5層構造を有し、双方の層Bは、二軸方向性のポリオレフィンをベースとする構造層を構成し、双方の層Cの各々は、変性ポリオレフィンをベースとする付着剤層を構成し、層Dは、40モル%以下のエチレンモル濃度を有するエチレン−ビニルアルコール共重合体をベースとする保護層を構成し、
少なくとも一方の層Bのポリオレフィンは、温度145℃以下で同時延伸により二軸方向性を付与された部分結晶性の熱可塑性ポリプロピレン及び/又は変性ポリプロピレンを構成することを特徴とする保護フィルム。Protective film for packaging in the form of a multilayer film based on a biaxially oriented polyolefin film with at least one functional or protective layer coextruded based on ethylene-vinyl alcohol copolymer (EVOH) In
Produced by co-extrusion of a co-extruded multilayer initial film, having an ethylene-vinyl alcohol copolymer layer with a thickness of at least 5 μm, an oxygen transmission rate (OTR; ASTM at a temperature of 23 ° C. and a relative humidity of 75% -3985) is less than 10 cm 3 / m 2 dbar,
Layer B / Layer C / Layer D / Layer C / Layer B have at least a five-layer structure, and both layers B constitute a structural layer based on biaxial polyolefin, Each comprises an adhesive layer based on a modified polyolefin, and layer D comprises a protective layer based on an ethylene-vinyl alcohol copolymer having an ethylene molar concentration of 40 mol% or less,
The protective film characterized in that the polyolefin of at least one layer B constitutes a partially crystalline thermoplastic polypropylene and / or modified polypropylene imparted with biaxiality by simultaneous stretching at a temperature of 145 ° C. or lower.
溶融物として必要な数の幅広スリットノズルから冷却ローラ上に初期多層フィルム層を構成する重合体を同時押出成形する工程と、延伸温度145℃以下かつ少なくとも10倍の面積拡大で、50%/秒以上の延伸速度を適用して、形成される初期多層フィルムに接触のない同時延伸を同時延伸装置により実行する工程とを含むことを特徴とする製造方法。In the manufacturing method of the protective film for packaging of any one of Claims 1-15,
50% / second by coextruding the polymer constituting the initial multilayer film layer on the cooling roller from the required number of wide slit nozzles as a melt, and at a stretching temperature of 145 ° C. or less and at least 10 times the area expansion Applying the above stretching speed and performing simultaneous stretching without contact with the initial multilayer film to be formed by a simultaneous stretching apparatus.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005025472A DE102005025472A1 (en) | 2005-06-02 | 2005-06-02 | Coextruded multilayer battery film with at least one ethylene-vinyl alcohol copolymer (EVOH) film layer, process for its preparation and its use |
DE102005025472.1 | 2005-06-02 | ||
PCT/EP2006/004726 WO2006128589A1 (en) | 2005-06-02 | 2006-05-18 | Coextruded multi-layer barrier film having at least one film ply of ethylene-vinyl alcohol copolymer (evoh), method of producing it, and its use |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2008545558A JP2008545558A (en) | 2008-12-18 |
JP4977694B2 true JP4977694B2 (en) | 2012-07-18 |
Family
ID=36691743
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2008513968A Active JP4977694B2 (en) | 2005-06-02 | 2006-05-18 | Multi-layer protective film co-extruded with a film layer comprising at least one ethylene-vinyl alcohol-copolymer (EVOH), method for producing the same and method for using the same |
Country Status (6)
Country | Link |
---|---|
US (2) | US20090208717A1 (en) |
EP (1) | EP1885558B2 (en) |
JP (1) | JP4977694B2 (en) |
AT (1) | ATE456995T1 (en) |
DE (2) | DE102005025472A1 (en) |
WO (1) | WO2006128589A1 (en) |
Families Citing this family (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102008014342A1 (en) | 2008-03-14 | 2009-10-01 | Roga Kg | Method for the production of tube like foil by extrusion, comprises decelerating and then accelerating flow speed of a coextrudate within an extrusion nozzle |
CA2751881C (en) * | 2009-02-27 | 2013-09-17 | Exxonmobil Oil Corporation | Plasma treated evoh multilayer film |
WO2011029950A1 (en) * | 2009-09-14 | 2011-03-17 | Cryovac, Inc. | Gas barrier heat-shrinkable film |
DE102010016850A1 (en) * | 2010-05-07 | 2011-11-10 | Südpack Verpackungen Gmbh & Co.Kg | Plastic film arrangement |
EP2468661A1 (en) * | 2010-12-23 | 2012-06-27 | Amcor Flexibles Kreuzlingen Ltd. | Bag-in-box package |
EP2720866B1 (en) | 2011-06-14 | 2018-01-10 | Essel Propack Limited | Partially opaque-partially clear laminates and methods thereof. |
SA112330849B1 (en) * | 2011-09-20 | 2017-10-12 | تترا لافال هولدينجز اند فاينانس اس.ايه | Multilayer barrier films, packaging laminates, and packaging container formed therefrom |
ITMI20112205A1 (en) * | 2011-12-02 | 2013-06-03 | Irplast Spa | PLASTIC FILMS |
ITMI20112204A1 (en) * | 2011-12-02 | 2013-06-03 | Irplast Spa | PLASTIC FILMS |
US20150210412A1 (en) * | 2012-09-04 | 2015-07-30 | Frederik Bergwerff | Method for packaging finished tobacco goods in a master box |
CN105143286B (en) | 2013-03-26 | 2017-09-15 | 博里利斯股份公司 | propylene copolymer with high impact property |
DE202013103437U1 (en) * | 2013-07-10 | 2013-09-20 | Flexopack S.A. | Thin foil for waste packaging cassettes |
KR101772370B1 (en) | 2014-05-22 | 2017-08-29 | 아사히 가세이 가부시키가이샤 | Heat-shrinkable laminate film |
TR201903982T4 (en) * | 2014-05-30 | 2019-04-22 | Irplast Spa | The use of plastic films for labels. |
KR101530160B1 (en) * | 2015-01-21 | 2015-06-19 | 임광명 | Protection Film Manufacturing Device and Method thereof |
US10807298B2 (en) | 2015-12-29 | 2020-10-20 | Whirlpool Corporation | Molded gas barrier parts for vacuum insulated structure |
CA2959423A1 (en) | 2016-03-10 | 2017-09-10 | Flexopack S.A. | Liner film |
DE102016210374A1 (en) * | 2016-06-10 | 2017-12-14 | Huhtamaki Flexible Packaging Germany Gmbh & Co. Kg | A sealable polyolefin film, a sealable polyolefin film package, and a method of making the sealable polyolefin film |
US11897231B2 (en) | 2016-06-15 | 2024-02-13 | Amcor Flexibles North America, Inc. | Package film having foil layers with intervening multilayer structure |
TWI580578B (en) * | 2016-07-06 | 2017-05-01 | 俊馳材料科技股份有限公司 | Cover Tape and Method for Manufacturing the same |
US11738927B2 (en) * | 2018-06-21 | 2023-08-29 | First Quality Tissue, Llc | Bundled product and system and method for forming the same |
US11697538B2 (en) * | 2018-06-21 | 2023-07-11 | First Quality Tissue, Llc | Bundled product and system and method for forming the same |
GB2577105B (en) | 2018-09-14 | 2022-04-06 | Innovia Films Ltd | Barrier film |
KR102201166B1 (en) * | 2018-09-21 | 2021-01-13 | 한국과학기술연구원 | Polyketone-based multi-layer film for packaging material and preparation method thereof |
IL295165A (en) * | 2020-01-31 | 2022-09-01 | Sesa Ambalaj Ve Plastik Sanayi Ticaret Anonim Sirketi | Recyclable retort package |
AU2021319883A1 (en) | 2020-08-06 | 2023-02-16 | Cryovac, Llc | Multilayer, coextruded polyolefin film and manufacture thereof on triple bubble lines |
AT525125B1 (en) * | 2021-06-02 | 2023-02-15 | Constantia Pirk Gmbh & Co Kg | Recyclable paper packaging laminate with a thin barrier film and good tear properties |
Family Cites Families (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NZ192416A (en) * | 1978-12-29 | 1981-10-19 | Kuraray Co | Ethylene-vinyl alcohol copolymer film which can be biaxially or multiaxially stretched |
CA1233739A (en) † | 1982-12-28 | 1988-03-08 | Mobil Oil Corporation | Barrier films |
DE3306189A1 (en) * | 1983-02-23 | 1984-08-23 | Hoechst Ag, 6230 Frankfurt | MULTILAYER FILM WITH A GAS AND AROMA BARRIER, METHOD FOR THEIR PRODUCTION AND THEIR USE |
EP0133188A1 (en) * | 1983-08-05 | 1985-02-20 | Brückner Maschinenbau Gernot Brückner GmbH & Co. KG | Process and apparatus for producing a hot-formed plastic composite |
US4561920A (en) * | 1984-02-08 | 1985-12-31 | Norchem, Inc. Formerly Northern Petrochemical Company | Biaxially oriented oxygen and moisture barrier film |
US4853602A (en) * | 1985-12-24 | 1989-08-01 | E. I. Dupont De Nemours And Company | System for using synchronous secondaries of a linear motor to biaxially draw plastic films |
EP0236099B2 (en) † | 1986-02-28 | 2004-12-01 | Cryovac, Inc. | Oxygen barrier packaging film |
JPH0813505B2 (en) * | 1987-04-30 | 1996-02-14 | 株式会社クラレ | Method for producing laminated stretched film |
US4990562A (en) † | 1987-08-24 | 1991-02-05 | E. I. Du Pont De Nemours And Company | Blends of ethylene vinyl alcohol copolymer and amorphous polyamide, and multilayer containers made therefrom |
US4880706A (en) * | 1987-10-05 | 1989-11-14 | Mobil Oil Corp. | Biaxially oriented multilayer barrier films |
JP2710844B2 (en) * | 1989-09-29 | 1998-02-10 | 株式会社クラレ | Ethylene-vinyl alcohol copolymer composition and multilayer structure |
CA2038800A1 (en) † | 1990-05-25 | 1991-11-26 | Gautam P. Shah | Ethylene propylene terpolymer film |
DE4421675A1 (en) * | 1994-06-23 | 1996-01-04 | 4 P Folie Forchheim Gmbh | Multilayer film |
US5759648A (en) † | 1996-07-05 | 1998-06-02 | Viskase Corporation | Multilayer plastic film, useful for packaging a cook-in foodstuff |
JPH10329286A (en) * | 1997-03-31 | 1998-12-15 | Toppan Printing Co Ltd | Polypropylene composite film material |
ATE263024T1 (en) * | 1998-12-18 | 2004-04-15 | Cryovac Inc | METHOD FOR PRODUCING A HIGHLY BIAXIALLY STRETCLED HEAT SHRINKABLE THERMOPLASTIC MULTI-LAYER FILM |
CA2310925C (en) * | 1999-06-11 | 2005-10-11 | Kuraray Co., Ltd. | Multilayered structure |
US20030211298A1 (en) * | 1999-12-30 | 2003-11-13 | Migliorini Robert A. | Multi-layer oriented polypropylene films with modified core |
EP1363771A2 (en) * | 2001-01-09 | 2003-11-26 | Exxonmobil Oil Corporation | Colored polyolefin film and method of making |
US7252878B2 (en) * | 2002-10-23 | 2007-08-07 | Toray Plastics (America), Inc. | High barrier flexible packaging structure |
AU2003298148B2 (en) * | 2002-11-29 | 2009-01-22 | Treofan Germany Gmbh & Co. Kg | Biaxially oriented film comprising a layer consisting of ethylene vinyl alcohol copolymer (EVOH) |
-
2005
- 2005-06-02 DE DE102005025472A patent/DE102005025472A1/en not_active Ceased
-
2006
- 2006-05-18 DE DE502006006077T patent/DE502006006077D1/en active Active
- 2006-05-18 US US11/921,308 patent/US20090208717A1/en not_active Abandoned
- 2006-05-18 WO PCT/EP2006/004726 patent/WO2006128589A1/en not_active Application Discontinuation
- 2006-05-18 AT AT06742982T patent/ATE456995T1/en active
- 2006-05-18 EP EP06742982A patent/EP1885558B2/en active Active
- 2006-05-18 JP JP2008513968A patent/JP4977694B2/en active Active
-
2011
- 2011-07-19 US US13/137,070 patent/US20110281096A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
US20110281096A1 (en) | 2011-11-17 |
DE502006006077D1 (en) | 2010-03-25 |
ATE456995T1 (en) | 2010-02-15 |
EP1885558B2 (en) | 2013-02-20 |
DE102005025472A1 (en) | 2006-12-07 |
JP2008545558A (en) | 2008-12-18 |
EP1885558B1 (en) | 2010-02-03 |
WO2006128589A1 (en) | 2006-12-07 |
US20090208717A1 (en) | 2009-08-20 |
EP1885558A1 (en) | 2008-02-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP4977694B2 (en) | Multi-layer protective film co-extruded with a film layer comprising at least one ethylene-vinyl alcohol-copolymer (EVOH), method for producing the same and method for using the same | |
US8178210B2 (en) | Multilayer oriented high-modulus film | |
CA2439578C (en) | Packaging films containing coextruded polyester and nylon layers | |
EP1749655B1 (en) | Multilayer Coextruded Films Including Frangible Intralaminar Bonding Forces | |
US8273447B2 (en) | Multilayer oriented film | |
JP2008540156A (en) | High-strength polypropylene-based protective film for packaging, its production and use | |
US9399318B2 (en) | High barrier heat sealable film with linear tear properties | |
US8642144B2 (en) | Innerliner with nylon skin layer | |
US20020009605A1 (en) | Polyester-containing biaxially-oriented polypropylene films | |
US20110039098A1 (en) | Gas-barrier films and sheets | |
KR20140063626A (en) | A multilayer barrier film, a packaging laminate comprising the film, a packaging container formed from the packaging laminate and a method for the production of the film | |
US20040144482A1 (en) | Thin film lamination-delamination process for fluoropolymers | |
US6872458B1 (en) | Biaxally-oriented polypropylene films containing a non-crystallizable, amorphous polyester layer, and method of making the same | |
US7563399B2 (en) | Biaxially oriented film having a layer consisting of ethylene-vinyl-alcohol copolymer (EVOH) | |
US20210354894A1 (en) | Recyclable Packaging Laminate Having A Good Barrier Effect And Low Density, And Method For The Production Thereof | |
RU2759719C1 (en) | Recyclable, easily ruptable packing multilayer material with good barrier effect and method for its production | |
JPH04232048A (en) | Ethylene propyrene terpolymer film | |
US20230311467A1 (en) | Enhanced Bag Drop Film and Packaging Using Oriented High-Density Polyethylene | |
AU2004261401B2 (en) | Multilayer oriented high-modulus film |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20090311 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20110906 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20111121 |
|
A602 | Written permission of extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A602 Effective date: 20111129 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20111228 |
|
A602 | Written permission of extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A602 Effective date: 20120116 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20120203 |
|
A602 | Written permission of extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A602 Effective date: 20120210 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20120306 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20120403 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20120416 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 4977694 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20150420 Year of fee payment: 3 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |